CN105241282A - Composite graphite heat exchanger - Google Patents

Composite graphite heat exchanger Download PDF

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Publication number
CN105241282A
CN105241282A CN201510592519.8A CN201510592519A CN105241282A CN 105241282 A CN105241282 A CN 105241282A CN 201510592519 A CN201510592519 A CN 201510592519A CN 105241282 A CN105241282 A CN 105241282A
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CN
China
Prior art keywords
heat exchange
exchange unit
graphite heat
graphite
heat exchanger
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Pending
Application number
CN201510592519.8A
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Chinese (zh)
Inventor
姚松年
朱天红
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NANTONG SHANJIAN GRAPHITE EQUIPMENTS CO Ltd
Original Assignee
NANTONG SHANJIAN GRAPHITE EQUIPMENTS CO Ltd
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Application filed by NANTONG SHANJIAN GRAPHITE EQUIPMENTS CO Ltd filed Critical NANTONG SHANJIAN GRAPHITE EQUIPMENTS CO Ltd
Priority to CN201510592519.8A priority Critical patent/CN105241282A/en
Publication of CN105241282A publication Critical patent/CN105241282A/en
Pending legal-status Critical Current

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Abstract

The invention discloses a composite graphite heat exchanger which comprises a cylinder, an upper sealing head and a lower sealing head. An upper tube plate is arranged between the cylinder and the upper sealing head. A lower tube plate is arranged between the cylinder and the lower sealing head. A graphite heat exchange unit I, a graphite heat exchange unit II and a row tube heat exchange unit are arranged inside the cylinder. Graphite plates are arranged between the graphite heat exchange unit I and the graphite heat exchange unit II as well as between the graphite heat exchange unit I and the row tube heat exchange unit respectively. A distributing chamber is formed between the graphite heat exchange unit II and the row tube heat exchange unit. An anti-scour plate is arranged at the lower end of the distributing chamber. A plurality of horizontal flow channels are formed in the graphite heat exchange unit I. A plurality of vertical flow channels are formed in the graphite heat exchange unit II. A plurality of heat exchange pipes are arranged inside the row tube heat exchange unit. The composite graphite heat exchanger is reasonable in structure and easy to operate. Compared with the prior art, the impact resistance of the heat exchanger is improved, and the heat transfer effect and the heat transfer efficiency are improved, so that the working efficiency is improved, and the production cost is reduced; meanwhile, the structure is excellent in corrosion resistance, and the service life of the heat exchanger is prolonged remarkably.

Description

A kind of composite graphite heat exchanger
Technical field
The present invention relates to a kind of graphite heat exchanger, be specifically related to a kind of composite graphite heat exchanger.
Background technology
Graphite heat exchanger is the heat exchanger that heat-transferring assembly graphite is made.The graphite manufacturing heat exchanger should have impermeability, conventional dipping class impermeable graphite and die mould impermeable graphite.Graphite heat exchanger can be divided into block Kong Shi ﹑ shell-and-tube and board-like 3 types by its structure.Block cellular type: the blocky graphite assembling components with holes by several forms.Shell-and-tube: shell-and-tube heat exchanger occupies critical role in graphite heat exchanger, is divided into again fixed and floating head type two kinds by structure.Board-like: plate type heat exchanger graphite cake bonding is made.In addition, Chen Jin Shi ﹑ fountain and bushing type etc. is also had.Graphite heat exchanger corrosion resistance and good, heat-transfer area is less scaling, and heat transfer property is good.But the easy embrittlement of graphite, bending resistance and tensile strength low, thus can only be used for low pressure, even if the block cavernous structure that bearing capacity is best, its operating pressure is generally also only 0.3 ~ 0.5 MPa.The cost of graphite heat exchanger is high, and volume is large, uses few.It is mainly used in the heat exchange of the Korrosionsmediums such as hydrochloric acid, sulfuric acid, acetic acid and phosphoric acid, as being used as the condenser etc. of acetic acid and acetic anhydride.
In order to save stainless steel and valuable nonferrous materials, graphite heat exchanger is widely used for the Korrosionsmediums such as process hydrochloric acid, sulfuric acid, acetic acid and phosphoric acid.Current graphite heat exchanger substantially divides two large class shell and tube and block cellular types structure.Tube-type graphite heat exchanger structure is simple, graphite material utilization rate is high, can be made into the equipment of larger heat transfer area, unit heat exchange area cost is lower than other version, but heat transfer efficiency is not as block cellular type, allow the pressure that uses lower, generally all not higher than 1Mpa, should not have intense impact, vibration and easily produce water hammer occasion under use.Block hole-type graphite heat exchanger table structure is firm, and having higher heat transfer system can improve operating pressure, is applicable to the occasion of thermal shock or vibration, but fluid resistance is comparatively large, and heat transfer area is little.
Therefore, for the problems referred to above, the present invention proposes a kind of new technical scheme.
Summary of the invention
The object of this invention is to provide a kind of shock-resistant, corrosion resistance strong, improves the compound double-effect graphite heat exchanger in service life.
The present invention is achieved through the following technical solutions:
A kind of composite graphite heat exchanger, comprises cylindrical shell, upper cover and low head, is provided with upper perforated plate between described cylindrical shell and upper cover, be provided with lower perforated plate between described cylindrical shell and low head, be provided with graphite heat exchange unit in described cylindrical shell , graphite heat exchange unit with tubulation heat exchange unit, described graphite heat exchange unit with graphite heat exchange unit and be provided with graphite cake between tubulation heat exchange unit, described graphite heat exchange unit and be provided with diffluence room between tubulation heat exchange unit, described diffluence room lower end is provided with impingement baffle, described graphite heat exchange unit on have some horizontal run, described graphite heat exchange unit on have some vertical run, be provided with some heat exchanger tubes in described tubulation heat exchange unit.
Further, be provided with deflection plate in described tubulation heat exchange unit, described deflection plate is spirality.
Further, described upper cover top is provided with material inlet, and upper cover side is provided with drain.
Further, described low head bottom is provided with material outlet, and low head side is provided with sewage draining exit.
Further, graphite heat exchange unit in described cylindrical shell side is provided with water inlet and delivery port.
The invention has the beneficial effects as follows: the present invention is rational in infrastructure, simple to operate, compared with prior art, improve the resistance to impact of heat exchanger, improve heat-transfer effect, and heat transfer efficiency, thus improve operating efficiency, saved production cost, meanwhile, this structure has excellent decay resistance, considerably improve the service life of heat exchanger, and this structural maintenance and easy maintenance, reduce the damage probability of heat exchanger.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Wherein: 1, cylindrical shell, 2, upper cover, 3, low head, 4, graphite heat exchange unit , 5, graphite heat exchange unit , 6, tubulation heat exchange unit, 7, horizontal run, 8, vertical run, 9, heat exchanger tube, 10, deflection plate, 11, impingement baffle, 12, diffluence room, 13, graphite cake, 14, material inlet, 15, material outlet, 16, water inlet, 17, delivery port, 18, upper perforated plate, 19, lower perforated plate, 20, drain, 21, sewage draining exit.
Detailed description of the invention
Illustrate below in conjunction with accompanying drawing and the present invention is described further.
A composite graphite heat exchanger as shown in Figure 1, comprises cylindrical shell 1, upper cover 2 and low head 3, is provided with upper perforated plate 18 between cylindrical shell 1 and upper cover 2, be provided with lower perforated plate 19 between cylindrical shell 1 and low head 3, be provided with graphite heat exchange unit in cylindrical shell 1 4, graphite heat exchange unit 5 and tubulation heat exchange unit 6, graphite heat exchange unit 4 with graphite heat exchange unit graphite cake 13 is provided with, graphite heat exchange unit between 5 and tubulation heat exchange unit 6 be provided with diffluence room 12 between 5 and tubulation heat exchange unit 6, diffluence room 12 lower end is provided with impingement baffle 11, graphite heat exchange unit some horizontal run 7 are had, graphite heat exchange unit on 4 have some vertical run on 5, in tubulation heat exchange unit 6, be provided with some heat exchanger tubes 9.Be provided with deflection plate 10 in tubulation heat exchange unit 6, deflection plate 10 is spirality, and upper cover 2 top is provided with material inlet 14, upper cover 14 side is provided with drain 20, low head 3 bottom is provided with material outlet 15, and low head 3 side is provided with sewage draining exit 21, graphite heat exchange unit in cylindrical shell 1 4 sides are provided with water inlet 16 and delivery port 17.
The present invention is rational in infrastructure, simple to operate, compared with prior art, improve the resistance to impact of heat exchanger, improve heat-transfer effect, and heat transfer efficiency, thus improve operating efficiency, saved production cost, meanwhile, this structure has excellent decay resistance, considerably improve the service life of heat exchanger, and this structural maintenance and easy maintenance, reduce the damage probability of heat exchanger.
The foregoing is only embodiments of the invention; not thereby the scope of the claims of the present invention is limited; every utilize description of the present invention and accompanying drawing content to do equivalent structure or equivalent flow process conversion; or be directly or indirectly used in other relevant technical fields, be all in like manner included in scope of patent protection of the present invention.

Claims (5)

1. a composite graphite heat exchanger, comprises cylindrical shell, upper cover and low head, is provided with upper perforated plate between described cylindrical shell and upper cover, is provided with lower perforated plate, it is characterized in that between described cylindrical shell and low head: be provided with graphite heat exchange unit in described cylindrical shell , graphite heat exchange unit with tubulation heat exchange unit, described graphite heat exchange unit with graphite heat exchange unit and be provided with graphite cake between tubulation heat exchange unit, described graphite heat exchange unit and be provided with diffluence room between tubulation heat exchange unit, described diffluence room lower end is provided with impingement baffle, described graphite heat exchange unit on have some horizontal run, described graphite heat exchange unit on have some vertical run, be provided with some heat exchanger tubes in described tubulation heat exchange unit.
2. a kind of composite graphite heat exchanger according to claim 1, it is characterized in that: be provided with deflection plate in described tubulation heat exchange unit, described deflection plate is spirality.
3. a kind of composite graphite heat exchanger according to claim 1, is characterized in that: described upper cover top is provided with material inlet, and upper cover side is provided with drain.
4. a kind of composite graphite heat exchanger according to claim 1, is characterized in that: described low head bottom is provided with material outlet, and low head side is provided with sewage draining exit.
5. a kind of composite graphite heat exchanger according to claim 1, is characterized in that: graphite heat exchange unit in described cylindrical shell side is provided with water inlet and delivery port.
CN201510592519.8A 2015-09-17 2015-09-17 Composite graphite heat exchanger Pending CN105241282A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510592519.8A CN105241282A (en) 2015-09-17 2015-09-17 Composite graphite heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510592519.8A CN105241282A (en) 2015-09-17 2015-09-17 Composite graphite heat exchanger

Publications (1)

Publication Number Publication Date
CN105241282A true CN105241282A (en) 2016-01-13

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CN201510592519.8A Pending CN105241282A (en) 2015-09-17 2015-09-17 Composite graphite heat exchanger

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CN (1) CN105241282A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106500538A (en) * 2016-12-16 2017-03-15 济南擎雷换热科技有限公司 A kind of double-flow band-tube type heat exchanger
CN108844390A (en) * 2018-07-19 2018-11-20 芜湖福民生物药业股份有限公司 Graphite heat exchanger
CN110715565A (en) * 2019-09-24 2020-01-21 浙江工程设计有限公司 Vertical integral drawable floating head heat exchanger suitable for non-clean fluid

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4850426A (en) * 1987-10-29 1989-07-25 Vicarb Gas/liquid heat exchanger with condensation
CN202547430U (en) * 2012-04-16 2012-11-21 南通苏宇化工设备制造有限公司 Graphite heat exchanger
CN202729789U (en) * 2012-07-26 2013-02-13 南通山剑石墨设备有限公司 Two-section heating type byproduct steam or hot water four-in-one hydrochloric acid synthesis furnace
CN203464819U (en) * 2013-08-21 2014-03-05 青岛鸿源换热器有限公司 Compound type graphite heat exchanger
CN105217572A (en) * 2015-09-18 2016-01-06 南通山剑石墨设备有限公司 Three sections of two-in-one synthetic furnaces of cooling type low temperature chlorination hydrogen

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4850426A (en) * 1987-10-29 1989-07-25 Vicarb Gas/liquid heat exchanger with condensation
CN202547430U (en) * 2012-04-16 2012-11-21 南通苏宇化工设备制造有限公司 Graphite heat exchanger
CN202729789U (en) * 2012-07-26 2013-02-13 南通山剑石墨设备有限公司 Two-section heating type byproduct steam or hot water four-in-one hydrochloric acid synthesis furnace
CN203464819U (en) * 2013-08-21 2014-03-05 青岛鸿源换热器有限公司 Compound type graphite heat exchanger
CN105217572A (en) * 2015-09-18 2016-01-06 南通山剑石墨设备有限公司 Three sections of two-in-one synthetic furnaces of cooling type low temperature chlorination hydrogen

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106500538A (en) * 2016-12-16 2017-03-15 济南擎雷换热科技有限公司 A kind of double-flow band-tube type heat exchanger
CN106500538B (en) * 2016-12-16 2019-04-19 山东擎雷环境科技股份有限公司 A kind of double-flow band-tube type heat exchanger
CN108844390A (en) * 2018-07-19 2018-11-20 芜湖福民生物药业股份有限公司 Graphite heat exchanger
CN110715565A (en) * 2019-09-24 2020-01-21 浙江工程设计有限公司 Vertical integral drawable floating head heat exchanger suitable for non-clean fluid

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