CN201364054Y - Overhead condenser - Google Patents

Overhead condenser Download PDF

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Publication number
CN201364054Y
CN201364054Y CNU2009200227024U CN200920022702U CN201364054Y CN 201364054 Y CN201364054 Y CN 201364054Y CN U2009200227024 U CNU2009200227024 U CN U2009200227024U CN 200920022702 U CN200920022702 U CN 200920022702U CN 201364054 Y CN201364054 Y CN 201364054Y
Authority
CN
China
Prior art keywords
tower body
sealing head
following
overhead condenser
grid spacer
Prior art date
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.)
Expired - Fee Related
Application number
CNU2009200227024U
Other languages
Chinese (zh)
Inventor
孙文勇
姚录田
许世林
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.)
SHANDONG DADI SALT CHEMICAL GROUP CO Ltd
Original Assignee
SHANDONG DADI SALT CHEMICAL GROUP CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SHANDONG DADI SALT CHEMICAL GROUP CO Ltd filed Critical SHANDONG DADI SALT CHEMICAL GROUP CO Ltd
Priority to CNU2009200227024U priority Critical patent/CN201364054Y/en
Application granted granted Critical
Publication of CN201364054Y publication Critical patent/CN201364054Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses an overhead condenser which belongs to a tube type heat exchanger widely applied to all fields in chemical engineering production. The overhead condenser comprises a tower body; an upper sealing head and a lower sealing head are arranged at the upper end and the lower end of the tower body respectively; the upper sealing head and the lower sealing head are communicated through a plurality of sealed tubes; a vapor inlet is formed on the upper sealing head, and a condensed water outlet is formed at the bottom end of the lower sealing head; and the tower body comprises an upper tower body and a lower tower body, and a U-shaped corrugated pipe expansion joint is arranged therebetween. The corrugated pipe expansion joint is arranged between the upper tower body and the lower tower body, thereby avoiding the damage of the heat exchanger due to stress stretching caused by different expansion coefficients; a cooling water inlet is formed on a lower tower body in a position near the lower sealing head, the cooling water is fed from the tail part and flows along the tubes, thereby slowing down the flow speed, increasing the exchanged heat, lowering the manufacturing cost, and reducing the weight of equipment under the condition of equal heat exchange efficiency.

Description

Overhead condenser
Technical field
The utility model relates to a kind of overhead condenser, belongs to tubular heat exchanger, is widely used in the every field of Chemical Manufacture.
Background technology
At present, the general shell-and-tube fixed head heat exchanger that adopts in trifluoro chlorine chrysanthemumic acid is produced, this heat exchanger comprises the tower body of integral type sealing, the two ends up and down of tower body are respectively equipped with upper cover and low head, tubulation by some sealings between described upper cover and the low head is communicated with, tubulation is fixed by stationary barrier, in use there have been various deficiencies in this heat exchanger, at first, the shell journey material and the front and back end temperature difference are big, shell coefficient of expansion difference easily causes heat exchanger to be subjected to stress fail in tension, and secondly this heat exchanger adopts stationary barrier to add strong turbulence, therefore increased the resistance that fluid passes through, strengthen the load of vavuum pump, simultaneously, between dividing plate, existed the turbulent flow dead angle, material is easily in this fouling, and the heat exchange efficiency of this kind heat exchanger is not high, increase the heat exchange area that exchange capability of heat must strengthen heat transmission equipment, thereby has increased the weight of equipment.
The utility model content
Problem to be solved in the utility model provides a kind of heat transfer efficiency height, and is applied widely, safe and reliable, makes simple overhead condenser.
For addressing the above problem, the utility model by the following technical solutions:
Overhead condenser, comprise tower body, the two ends up and down of described tower body are respectively equipped with upper cover and low head, tubulation by some sealings between described upper cover and the low head is communicated with, described upper cover is provided with steam inlet, the bottom of described low head is provided with condensation-water drain, it is characterized in that: described tower body is made of last tower body and following tower body, and described going up between tower body and the following tower body is provided with U type bellows expansion joint.
Below be to further improvement in the technical proposal:
Described going up is provided with the last grid spacer that tubulation can be located in the tower body, following tower body is provided with down grid spacer, and last grid spacer and following grid spacer are semicircle, have reduced the turbulent flow between last grid spacer and the following grid spacer, have reduced the load of vavuum pump.
The described grid spacer that goes up is oppositely arranged on tower body with following grid spacer, reduced existing the turbulent flow dead angle between dividing plate, thereby material is difficult in this fouling.
Described position of going up close upper cover on the tower body is provided with coolant outlet and exhaust outlet, position near low head on the following tower body is provided with cooling water inlet and discharge outlet, cooling water is taked from the mode of afterbody charging, and cooling water flows along tubulation and reduced flow velocity, has increased heat exchange.
Use technique scheme, the beneficial effects of the utility model, be provided with bellows expansion joint between last tower body and the following tower body, prevented that the shell journey coefficient of expansion difference from causing heat exchanger to be subjected to stress fail in tension, the position near low head on the following tower body is provided with cooling water inlet, and cooling water is taked from the mode of afterbody charging, cooling water flows along tubulation and has reduced flow velocity, increased heat exchange, it is low to have reduced manufacturing expense, has reduced the weight of equipment under the situation of equal heat exchange efficiency.
Come the technical solution of the utility model is further described below in conjunction with drawings and Examples:
Description of drawings
Accompanying drawing 1 is the structural representation of overhead condenser among the utility model embodiment;
Accompanying drawing 2 is that the A-A of Fig. 1 is to cutaway view.
Grid spacer, 6-cooling water inlet, 7-condensation-water drain, 8-discharge outlet, 9-support, 10-dividing plate, the last grid spacer of 11-, 12-coolant outlet, 13-upper cover, 14-low head, 15-exhaust outlet, 16-flange under 1-steam inlet, 2-tower body, 3-tubulation, 4-corrugated expansion pipe joint, the 5-.
The specific embodiment
Embodiment, as accompanying drawing 1, shown in 2, overhead condenser, comprise tower body 2, the two ends up and down of described tower body 2 are respectively equipped with upper cover 13 and low head 14, described upper cover 13 is connected with tower body 2 with dividing plate 10 by flange 16 respectively with low head 14, dividing plate 10 is with upper cover 13, low head 14 is divided into 3 chambers with tower body 2, described upper cover 13 is provided with steam inlet 1, the bottom of described low head 14 is provided with condensation-water drain 7, described tower body 2 comprises tower body and following tower body, on described, connect by bellows expansion joint 4 between the following tower body, tubulation 3 by some sealings between described upper cover 13 and the low head 14 is communicated with, be provided with support 9 around the described upward tower body, described going up is provided with the last grid spacer 11 that tubulation can be located in the tower body, and following tower body is provided with down grid spacer 5, the described grid spacer 11 that goes up is semicircle with following grid spacer 5, and last grid spacer 11 is oppositely arranged with following grid spacer 5; Described position of going up close upper cover 13 on the tower body is provided with coolant outlet 12 and exhaust outlet 15, and the position near low head 14 on the following tower body is provided with cooling water inlet 6 and discharge outlet 8.
Be provided with U type bellows expansion joint 4 between last tower body and the following tower body, prevented that the shell journey coefficient of expansion difference from causing heat exchanger to be subjected to stress fail in tension, position near low head on the following tower body is provided with cooling water inlet 6, cooling water 6 is taked from the mode of afterbody charging, cooling water flows along tubulation and has reduced flow velocity, increased heat exchange, it is low to have reduced manufacturing expense, has reduced the weight of equipment under the situation of equal heat exchange efficiency.

Claims (4)

1, overhead condenser, the tower body (2) that comprises sealing, the two ends up and down of described tower body (2) are respectively equipped with upper cover (13) and low head (14), tubulation (3) by some sealings between described upper cover (13) and the low head (14) is communicated with, described upper cover (14) is provided with steam inlet, described low head (13) is provided with condensation-water drain (7), it is characterized in that: described tower body (2) is made of last tower body and following tower body, and described going up between tower body and the following tower body is provided with U type bellows expansion joint (4).
2, overhead condenser as claimed in claim 1, it is characterized in that: described going up is respectively equipped with last grid spacer (11) and the following grid spacer (5) that tubulation (3) can be located on tower body and the following tower body, described upward grid spacer (11) and following grid spacer (5) are semicircle.
3, overhead condenser as claimed in claim 2 is characterized in that: go up grid spacer (11) and be oppositely arranged with following grid spacer (5).
4, overhead condenser as claimed in claim 1, it is characterized in that: described position of going up close upper cover (13) on the tower body is provided with coolant outlet (12) and exhaust outlet (15), and the position near low head (14) on the following tower body is provided with cooling water inlet (6) and discharge outlet (8).
CNU2009200227024U 2009-03-02 2009-03-02 Overhead condenser Expired - Fee Related CN201364054Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2009200227024U CN201364054Y (en) 2009-03-02 2009-03-02 Overhead condenser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2009200227024U CN201364054Y (en) 2009-03-02 2009-03-02 Overhead condenser

Publications (1)

Publication Number Publication Date
CN201364054Y true CN201364054Y (en) 2009-12-16

Family

ID=41474723

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2009200227024U Expired - Fee Related CN201364054Y (en) 2009-03-02 2009-03-02 Overhead condenser

Country Status (1)

Country Link
CN (1) CN201364054Y (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101893394A (en) * 2010-07-28 2010-11-24 郭心岭 Thread aluminum pipe heat exchanger
CN102679755A (en) * 2012-05-30 2012-09-19 苏州市金翔钛设备有限公司 Self-cleaning type high-efficiency tower top condenser
CN102679809A (en) * 2012-05-29 2012-09-19 苏州市金翔钛设备有限公司 Self-cleaning type overhead condenser
CN102679797A (en) * 2012-05-29 2012-09-19 苏州市金翔钛设备有限公司 Novel overhead condenser
CN102706210A (en) * 2012-05-29 2012-10-03 苏州市金翔钛设备有限公司 Overhead condenser
CN102764079A (en) * 2012-07-23 2012-11-07 山西瑞飞机械制造有限公司 Full-automatic environmental-friendly energy-saving pulp cooking unit

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101893394A (en) * 2010-07-28 2010-11-24 郭心岭 Thread aluminum pipe heat exchanger
CN101893394B (en) * 2010-07-28 2012-08-08 郭心岭 Thread aluminum pipe heat exchanger
CN102679809A (en) * 2012-05-29 2012-09-19 苏州市金翔钛设备有限公司 Self-cleaning type overhead condenser
CN102679797A (en) * 2012-05-29 2012-09-19 苏州市金翔钛设备有限公司 Novel overhead condenser
CN102706210A (en) * 2012-05-29 2012-10-03 苏州市金翔钛设备有限公司 Overhead condenser
CN102679755A (en) * 2012-05-30 2012-09-19 苏州市金翔钛设备有限公司 Self-cleaning type high-efficiency tower top condenser
CN102764079A (en) * 2012-07-23 2012-11-07 山西瑞飞机械制造有限公司 Full-automatic environmental-friendly energy-saving pulp cooking unit

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20091216

Termination date: 20100302