CN103884201A - Internally-installed plate-shell type overhead condenser for solvent regeneration tower - Google Patents
Internally-installed plate-shell type overhead condenser for solvent regeneration tower Download PDFInfo
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- CN103884201A CN103884201A CN201410041123.XA CN201410041123A CN103884201A CN 103884201 A CN103884201 A CN 103884201A CN 201410041123 A CN201410041123 A CN 201410041123A CN 103884201 A CN103884201 A CN 103884201A
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Abstract
The invention discloses an internally-installed plate-shell type overhead condenser for a solvent regeneration tower. The condenser can be installed in the solvent regeneration tower, a condensed liquid-phase medium can flow back to the top of the tower by means of natural backflow, and arrangement is technically simple. Heat exchange plates of the condenser are made of titanium and resistant to corrosion, so that equipment replacement frequency can be greatly lowered, mounting cost and maintenance cost of the condenser can be reduced maximally, and safety and reliability in long-time operation of the condenser can be guaranteed. The plate-shell type condenser comprises a shell and a plate core, the plate core is formed by laminating and fixedly connecting the plurality of heat exchange plates, and the shell is provided with an overhead gas inlet, a circulating water inlet, a circulating water outlet, a condensate outlet and an acid gas outlet. Cooling of overhead gas is realized by cooperation of a plate side runner and a shell side runner of the plate core.
Description
Technical field
The present invention relates to a kind of lamella heat exchanger, be specifically related to the built-in shell-and-plate condenser of a kind of solvent reclamation tower top, belong to heat transfer unit (HTU) technical field.
Background technology
Solvent regeneration tower adopts the rectifying column configuration of fractional distilling tube, liquid phase infinite reflux, enter most of sour gas that the rich solution of solvent regeneration tower contains resolves in tower, then the reboiler that enters regenerator bottom is further heated desorb, and solvent liquid is fully regenerated.A large amount of gas phase medias of tower top are cooled to liquid phase by refrigerant in overhead condenser simultaneously, then by the mode of natural back flow or forced refluence, the liquid phase medium of condensation are back to tower top.Natural back flow is to utilize high potential difference between overhead condenser and tower refluxing opening to realize the backflow of cooling medium; Forced refluence adopts pump that transmitting power is provided.
Existing regeneration overhead condenser is deposited deficiency both ways: (1) forced refluence mode technology arrangement complexity; Although natural back flow technological process is relatively simple, the bearing height of overhead condenser will be far above the overhead condenser of forced refluence, need to build corresponding building and support, thereby bring extra-pay; And require condensation vessel volume little, lightweight.(2) overhead condenser seriously corroded.The CO that regenerator overhead gas mainly produces
2-H
2s-H
2o can make condenser occur the phenomenons such as homogeneous corrosion, hydrogen blister, hydrogen embrittlement and stress corrosion cracking, causes condenser seriously corroded, and service life is short, and inspect and change is frequent, and maintenance of equipment expense is raise, and has reduced the production capacity of whole device.
Summary of the invention
In view of this, the invention provides the built-in shell-and-plate condenser of a kind of solvent reclamation tower top, this condensation vessel volume is little, lightweight, can directly support and be arranged on regenerator inside, the liquid phase medium of condensation is back to tower top by employing natural back flow mode, and heat exchange plate employing titanium material, can greatly reduce the replacement frequency of equipment, reduce to greatest extent mounting cost and the maintenance cost of device, and assurance device long period safe and reliable operation.
This shell-and-plate condenser comprises: housing and plate core body; Described plate core body comprises that two with upper sheet space pair, and described plate is to being made up of two identical sheet annular heat exchange plates of structure; The surface distributed of described heat exchange plate has projection, and on its ring surface, is processed with two circular holes, and two circular holes on two heat exchange plate ring surfaces are welded together to form respectively to plate pair; Two with upper sheet space to coaxial placement, by the welding of inner circle right adjacent two plates and cylindrical, form plate core body respectively.In plate core body, between the centre bore of plate core body and each plate centering two plates, passage forms shell side passage, the circular hole of plate core body centre bore both sides and plate pair and plate between runner formation plate journey runner.
Described plate core body is fixedly mounted on enclosure interior, and the annular space between plate core body and housing is gas-liquid separation space; On a side end face of described housing: processing column top gas entrance in circular hole position in plate core body, described tower overhead gas entrance and shell side passage connect; On plate core body ring surface, two positions corresponding to circular hole respectively arrange an ozzle, are used separately as recirculated water entrance and circulating water outlet, and described recirculated water entrance and circulating water outlet and plate journey runner connect, the sealed bottom of plate journey runner; On this side end face of housing, process sour gas outlet simultaneously; On the end face of described housing opposite side, process condensate outlet; Described sour gas outlet and condensate outlet connect with gas-liquid separation space respectively.
The diameter of described housing is the more than 1.5 times of plate core diameter.
On described housing, be provided with two condensate outlets, two condensate outlets are connected with the two ends of T shape overflow pipe horizontal component respectively, and liquid seal device is stretched in the bottom of T shape overflow pipe vertical portion.
The surface uniform of described heat exchange plate is distributed with arc fin, is corrugated.
The surface uniform of described heat exchange plate is distributed with the protruding and ball impression of ball; Form plate to time, the ball impression of two heat exchange plate opposite faces is corresponding with ball impression, ball is protruding protruding corresponding with ball.
Protruding and degree of depth ball impression of described ball is 2～5 millimeters, and diameter is 8～15 millimeters.
Described heat exchange plate is titanium plate.
Beneficial effect
(1) lamella heat exchanger of this kind of version can be arranged as built-in cold condenser in regeneration overhead, adopts natural back flow mode that the liquid phase medium of condensation is back to tower top, and technological process is simple.And because lamella heat exchanger adopts titanium plate, good corrosion resistance, can greatly reduce the replacement frequency of equipment, reduces to greatest extent mounting cost and the maintenance cost of device, and assurance device long period safe and reliable operation.
(2) at condensate outlet, overflow pipe and liquid seal device are set, guarantee condensate liquid can be discharged heat-exchange tube smoothly, prevents thermal medium gas backflow in tower simultaneously.
(3) heat exchange plate adopts the corrugated plating can enhanced heat exchange, and heat exchange efficiency is high.
(4) heat exchange plate adopts fourth born of the same parents plate, and the runner of the plate core body forming is thus more unimpeded, can reduce flow resistance, increases rate of flow of fluid, reduces equipment scaling, and the while is clean and maintenance easily, improves reliability and the life-span of equipment.
Brief description of the drawings
Fig. 1 is the built-in condenser structure schematic diagram of tower top;
Fig. 2 is the structural representation of the first hot plate sheet;
Fig. 3 is the structural representation of the second hot plate sheet;
Runner schematic diagram when Fig. 4 is the second hot plate sheet formation plate core body;
Fig. 5 is the structural representation of condenser;
Fig. 6 is condenser internal flow schematic diagram.
Wherein, 1-housing, 2-recirculated water entrance, the outlet of 3-sour gas, 4-circulating water outlet, 5-tower overhead gas entrance, 6-plate core body, 7-condensate outlet.
Detailed description of the invention
Below in conjunction with drawings and Examples, the specific embodiment of the present invention is further described, following examples are only for technical scheme of the present invention is more clearly described, and can not limit the scope of the invention with this.
The present embodiment provides a kind of solvent reclamation tower top built-in shell-and-plate condenser, comprises housing 1 and plate core body 6, and plate core body 6 is by stacked affixed rear formation of multiple heat exchange plates.Described heat exchange plate is sheet loop configuration, is processed with two circular holes on the ring surface of heat exchange plate, and described two circular holes are arranged in the bilateral symmetry of heat exchange plate inner circle.In the present embodiment, provide the version of two kinds of heat exchange plates, as shown in Figures 2 and 3.Heat exchange plate shown in Fig. 2 is corrugated plating, is distributed with arc fin at the surface uniform of heat exchange plate, forms corrugated.Heat exchange plate shown in Fig. 3 is fourth born of the same parents plates, the surface uniform of heat exchange plate be intervally distributed with ball impression of the same size and ball protruding, protruding and degree of depth ball impression of ball is 2～5 millimeters, diameter is 8～15 millimeters.
In the time that heat exchange plate is corrugated plating, the generation type of plate core body is: two heat exchange plates are coaxially placed, and respectively the circular hole of same position on two heat exchange plate ring surfaces is welded together, and forms plate pair; Then by multiple plates to coaxial placement, respectively right adjacent two plates inner circle and cylindrical are welded together, form plate core body 6.Between the centre bore of plate core body 6 and each plate centering two plates, passage forms shell side passage, the circular hole of plate core body 6 centre bore both sides and plate pair and plate between runner formation plate journey runner.
When heat exchange plate is fourth born of the same parents plates, the generation type of plate core body is: two heat exchange plates are coaxially placed, and makes the ball impression of two heat exchange plate opposite faces corresponding with ball impression, and ball is protruding protruding corresponding with ball.So on latter two heat exchange plate ring surface, the circular hole of same position welds together, and forms plate pair; Finally by multiple plates to coaxial placement, respectively right adjacent two plates inner circle and cylindrical are welded together, form plate core body 6.In the plate core body 6 forming, be ball impression corresponding with ball impression in the opposite face of any two adjacent plate, ball is protruding protruding corresponding with ball; As shown in Figure 4.Between the centre bore of plate core body 6 and each plate centering two plates, passage forms shell side passage, the circular hole of plate core body 6 centre bore both sides and plate pair and plate between runner formation plate journey runner.
The structure of housing 1 as shown in Figure 5, the column construction that housing 1 is hollow, plate core body 6 is coaxially fixedly mounted on housing 1 inside, the upper and lower surface of plate core body 6 is conflicted with the inner surface up and down of housing 1 respectively, for ensureing the isolation of plate journey runner and shell side runner, be positioned on the ring surface of plate core body 6 bottom heat exchange plates and do not process circular hole, make the sealed bottom of plate journey runner.The diameter of housing 1 is 2 times of plate core body 6 diameters, and the space forming between plate core body 6 outer circumference surfaces and housing 1 inner peripheral surface is thus gas-liquid separation space.Upper surface at housing 1: plate core body 6 centre bore positions coaxially process circular hole as tower overhead gas entrance 5, tower overhead gas entrance 5 connects with the shell side runner of plate core body 6; Ozzle of the each coaxial processing in position that plate core body 6 centre bore two mother rib lateral rotundums are corresponding, is used separately as recirculated water entrance 2 and circulating water outlet 4, and recirculated water entrance 2 and circulating water outlet 4 connect with the plate journey runner of plate core body 6.In two sour gas outlets 3 of upper surface processing of housing 1, the lower surface of housing 1 is processed with two condensate outlets 7 simultaneously, and described sour gas outlet and condensate outlet all connect with gas-liquid separation space.
When use, this condenser is directly installed on to the top in regenerator, and supports by the regenerator after reinforcing.Two condensate outlets of condenser bottom are connected with the two ends of T shape overflow pipe horizontal component respectively, as shown in Figure 1.Discharge opeing is the key that condensing plant can run well, if can not quick fluid-discharge, hydrops can flood part plate bundle, reduces effective heat transfer area of heat exchanger; For this reason, in the bottom of overflow pipe vertical portion, liquid seal device is set, to ensure that condensate liquid can discharge heat-exchange tube smoothly.The fluid-tight of certain altitude simultaneously can also prevent thermal medium gas backflow in tower.
The operation principle of this condenser is as shown in Fig. 1 and Fig. 6: in regenerator, thermal medium (being tower overhead gas) rises at the bottom of tower, rises to tower top through lower resistance part, enters the shell side runner of condenser from tower overhead gas entrance 5; Cold medium is cooling water, enters the plate journey runner of condenser from recirculated water entrance 2, flows out from circulating water outlet 4.The cooling water of plate journey runner and the tower overhead gas of shell side runner form cross-current, take away latent heat and sensible heat that tower overhead gas discharges, and it is condensate liquid that tower overhead gas is condensed into liquid state.The gas-liquid separation space of the two-phase fluid of condensation between plate core body 6 and housing 1 separates.Condensate liquid is gravitate in housing, enters overflow pipe by condensate outlet, is back to tower tray.Sour gas, after gas-liquid separation, is discharged from sour gas outlet 3.
In order to ensure the reliability of condenser, should make two media (tower overhead gas and cooling water) not contact, do not leak, equipment must seal closely.This condenser heat transfer element is titanium plate (being that heat exchange plate is titanium plate), between two plates, is welded and is formed plate core by fully-automatic laser.Use full-welding plate-type version, make this condenser in performance heat-exchangers of the plate type efficient heat transfer performance, ensured sealing property, improved bearing capacity, device security is reliable.
The above is only the preferred embodiment of the present invention; it should be pointed out that for those skilled in the art, do not departing under the prerequisite of the technology of the present invention principle; can also make some improvements and modifications, these improvements and modifications also should be considered as protection scope of the present invention.
Claims (7)
1. the built-in shell-and-plate condenser of solvent reclamation tower top, is characterized in that, comprising: housing (1) and plate core body (6); Described plate core body (6) comprises that two with upper sheet space pair, and described plate is to being made up of two identical sheet annular heat exchange plates of structure; The surface distributed of described heat exchange plate has projection, and on its ring surface, is processed with two circular holes, and two circular holes on two heat exchange plate ring surfaces are welded together to form respectively to plate pair; Two with upper sheet space to coaxial placement, by the welding of inner circle right adjacent two plates and cylindrical, form plate core body (6) respectively; In plate core body (6), between the centre bore of plate core body (6) and each plate centering two plates, passage forms shell side passage, the circular hole of plate core body (6) centre bore both sides and plate pair and plate between runner formation plate journey runner;
Described plate core body (6) is fixedly mounted on housing (1) inside, and the annular space between plate core body (6) and housing (1) is gas-liquid separation space; On a side end face of described housing (1): circular hole position processing column top gas entrance (5) in plate core body (6), described tower overhead gas entrance (5) connects with shell side passage; On plate core body (6) ring surface, two positions corresponding to circular hole respectively arrange an ozzle, be used separately as recirculated water entrance (2) and circulating water outlet (4), described recirculated water entrance (2) and circulating water outlet (4) connect with plate journey runner, the sealed bottom of plate journey runner; On this side end face of housing (1), process sour gas outlet (3) simultaneously; On the end face of described housing (1) opposite side, process condensate outlet (7); Described sour gas outlet (3) and condensate outlet (7) connect with gas-liquid separation space respectively.
2. the built-in shell-and-plate condenser of solvent reclamation tower top as claimed in claim 1, is characterized in that, the diameter of described housing (1) is the more than 1.5 times of plate core body (6) diameter.
3. the built-in shell-and-plate condenser of solvent reclamation tower top as claimed in claim 1, it is characterized in that, on described housing (1), be provided with two condensate outlets, two condensate outlets are connected with the two ends of T shape overflow pipe horizontal component respectively, and liquid seal device is stretched in the bottom of T shape overflow pipe vertical portion.
4. the built-in shell-and-plate condenser of solvent reclamation tower top as claimed in claim 1, is characterized in that, the surface uniform of described heat exchange plate is distributed with arc fin, is corrugated.
5. the built-in shell-and-plate condenser of solvent reclamation tower top as claimed in claim 1, is characterized in that, the surface uniform of described heat exchange plate is distributed with the protruding and ball impression of ball; Form plate to time, the ball impression of two heat exchange plate opposite faces is corresponding with ball impression, ball is protruding protruding corresponding with ball.
6. the built-in shell-and-plate condenser of solvent reclamation tower top as claimed in claim 1, is characterized in that, protruding and degree of depth ball impression of described ball is 2～5 millimeters, and diameter is 8～15 millimeters.
7. the built-in shell-and-plate condenser of solvent reclamation tower top as claimed in claim 1, is characterized in that, described heat exchange plate is titanium plate.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201410041123.XA CN103884201B (en) | 2014-01-27 | 2014-01-27 | The built-in shell-and-plate condenser of solvent reclamation tower top |
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| CN201410041123.XA CN103884201B (en) | 2014-01-27 | 2014-01-27 | The built-in shell-and-plate condenser of solvent reclamation tower top |
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| CN103884201B CN103884201B (en) | 2016-05-04 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104197736A (en) * | 2014-09-09 | 2014-12-10 | 浙江建业化工股份有限公司 | Solvent regeneration tower top condensing system and lamella heat exchanger used in same |
| CN105423782A (en) * | 2015-12-09 | 2016-03-23 | 上海齐耀热能工程有限公司 | Rich and lean solution heat exchanger for low-temperature methanol washing process |
| CN106949751A (en) * | 2017-04-26 | 2017-07-14 | 宁夏凤城永生锅炉有限公司 | Dehydrogenation overhead condenser |
| CN108871003A (en) * | 2018-08-10 | 2018-11-23 | 江苏永大化工设备有限公司 | A kind of Novel unpowered integrated condensing separator |
| CN115289866A (en) * | 2022-07-21 | 2022-11-04 | 无锡市张泾压力容器制造有限公司 | Tower top built-in plate shell type condenser |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1608193A (en) * | 2001-12-27 | 2005-04-20 | 瓦特鲁斯公司 | Heat exchange of a round plate heat exchanger |
| CN202188783U (en) * | 2011-07-05 | 2012-04-11 | 齐力制冷系统(深圳)有限公司 | Heat interchange core body |
| CN202582237U (en) * | 2012-04-10 | 2012-12-05 | 甘肃蓝科石化高新装备股份有限公司 | Plate-shell type condenser |
| CN103063067A (en) * | 2011-10-21 | 2013-04-24 | 中国科学院过程工程研究所 | Graded heat exchange distributed control phase-change heat transfer system and heat transfer method |
| CN203798189U (en) * | 2014-01-27 | 2014-08-27 | 中国船舶重工集团公司第七一一研究所 | Overhead built-in shell-and-plate type condenser of solvent regeneration tower |
-
2014
- 2014-01-27 CN CN201410041123.XA patent/CN103884201B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1608193A (en) * | 2001-12-27 | 2005-04-20 | 瓦特鲁斯公司 | Heat exchange of a round plate heat exchanger |
| CN202188783U (en) * | 2011-07-05 | 2012-04-11 | 齐力制冷系统(深圳)有限公司 | Heat interchange core body |
| CN103063067A (en) * | 2011-10-21 | 2013-04-24 | 中国科学院过程工程研究所 | Graded heat exchange distributed control phase-change heat transfer system and heat transfer method |
| CN202582237U (en) * | 2012-04-10 | 2012-12-05 | 甘肃蓝科石化高新装备股份有限公司 | Plate-shell type condenser |
| CN203798189U (en) * | 2014-01-27 | 2014-08-27 | 中国船舶重工集团公司第七一一研究所 | Overhead built-in shell-and-plate type condenser of solvent regeneration tower |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104197736A (en) * | 2014-09-09 | 2014-12-10 | 浙江建业化工股份有限公司 | Solvent regeneration tower top condensing system and lamella heat exchanger used in same |
| CN104197736B (en) * | 2014-09-09 | 2016-06-22 | 浙江建业化工股份有限公司 | Solvent regeneration tower tower top condensing system and lamella heat exchanger used |
| CN105423782A (en) * | 2015-12-09 | 2016-03-23 | 上海齐耀热能工程有限公司 | Rich and lean solution heat exchanger for low-temperature methanol washing process |
| CN105423782B (en) * | 2015-12-09 | 2017-07-28 | 上海齐耀热能工程有限公司 | Low-temp methanol washing process poor rich liquid heat exchanger |
| CN106949751A (en) * | 2017-04-26 | 2017-07-14 | 宁夏凤城永生锅炉有限公司 | Dehydrogenation overhead condenser |
| CN108871003A (en) * | 2018-08-10 | 2018-11-23 | 江苏永大化工设备有限公司 | A kind of Novel unpowered integrated condensing separator |
| CN115289866A (en) * | 2022-07-21 | 2022-11-04 | 无锡市张泾压力容器制造有限公司 | Tower top built-in plate shell type condenser |
| CN115289866B (en) * | 2022-07-21 | 2024-03-19 | 无锡市张泾压力容器制造有限公司 | Built-in lamella condenser in top of tower |
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| CN103884201B (en) | 2016-05-04 |
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Address after: 201108 Shanghai city Minhang District Huaning Road No. 3111 Patentee after: The 711 Research Institute of China Shipbuilding Corp. Address before: 201108 Shanghai city Minhang District Huaning Road No. 3111 Patentee before: Shanghai Marine Diesel Engine Research Institute |