CN202238019U - Auxiliary heater of pre-reactor in low-temperature hydrogenation and benzene-production process - Google Patents

Auxiliary heater of pre-reactor in low-temperature hydrogenation and benzene-production process Download PDF

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Publication number
CN202238019U
CN202238019U CN2011203044200U CN201120304420U CN202238019U CN 202238019 U CN202238019 U CN 202238019U CN 2011203044200 U CN2011203044200 U CN 2011203044200U CN 201120304420 U CN201120304420 U CN 201120304420U CN 202238019 U CN202238019 U CN 202238019U
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CN
China
Prior art keywords
reactor
auxiliary heater
heater
temperature hydrogenation
model
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 - Lifetime
Application number
CN2011203044200U
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Chinese (zh)
Inventor
夏潍平
魏建华
王读福
丁亮
钟经民
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.)
WEIFANG ZHENXING RISHENG CHEMICAL CO Ltd
Original Assignee
WEIFANG ZHENXING RISHENG CHEMICAL 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
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Priority to CN2011203044200U priority Critical patent/CN202238019U/en
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Publication of CN202238019U publication Critical patent/CN202238019U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model provides an auxiliary heater of a pre-reactor in a low-temperature hydrogenation and benzene-production process, comprising an auxiliary heater body, wherein the auxiliary heater body is arranged on an inlet pipeline of the pre-reactor and comprises a heat-conducting oil heater provided with an adjusting valve. The auxiliary heater provided in the utility model has the advantages of a simple structure, convenience and reliability in adjustment and capability of meeting heat requirements of the pre-reactor in each time period; and meanwhile, the load of an electric heater is reduced, the service life of the electric heater is prolonged and electricity consumption amounts are reduced, so that the processing cost of products is reduced.

Description

The auxiliary heater of pre-reactor in a kind of low temperature hydrogenation system benzene process
Technical field
The utility model relates to a kind of heater, is specifically related to the auxiliary heater of pre-reactor in a kind of low temperature hydrogenation system benzene process.
Background technology
In the present low temperature hydrogenation system benzene technology; The thermal source of pre-reactor mainly comes from electric heater and evaporimeter reboiler; But often satisfied not the heating requirements of pre-reactor; Especially when main device is driven parking and catalyst regeneration heating, depend merely on the thermal source of electric heater and evaporimeter, satisfied not the well-defined reaction temp requirement of pre-reactor far away; And when normal operation, the load of electric heater is very big, and the running of high load capacity can be shortened the service life of electric heater, increases power consumption, improves the product processing charges.
The utility model content
The utility model technical problem to be solved provides the auxiliary heater of pre-reactor in a kind of low temperature hydrogenation system benzene process; It is simple in structure; Can satisfy the heat demand in each stage of pre-reactor, reduce the load of electric heater, thereby eliminate defective in the above-mentioned background technology.
For realizing above-mentioned purpose, the utility model adopts following technical scheme:
The auxiliary heater of pre-reactor comprises the auxiliary heater body in a kind of low temperature hydrogenation system benzene process, it is characterized in that, said auxiliary heater body is arranged on the inlet pipeline of said pre-reactor.
As a kind of improvement, said auxiliary heater body comprises hotline heater.
As a kind of further improvement, said hotline heater is provided with the adjusting device that is used to regulate the conduction oil flow.
As a kind of further improvement, said adjusting device comprises control valve.
Owing to adopted above structure, the utlity model has following beneficial effect:
Install the auxiliary heater body additional on the pre-reactor inlet pipeline of the utility model after the outlet of unstripped gas superheater; Extraly heat is provided for pre-reactor; Can satisfy the heat demand of each time period of pre-reactor; Heat demand when for example main device is driven parking and catalyst regeneration heating, and reduced dependence to electric heater and evaporimeter thermal source, reduced the load of electric heater simultaneously.
The auxiliary heater body of the utility model comprises that install adjustment valve can be controlled the material temperature that gets into pre-reactor through the flow of regulating conduction oil as the hotline heater of adjusting device on it, and is safe and reliable.
Can know that to sum up the utility model is simple in structure, easy to adjust reliable; Can satisfy the heat demand of each time period of pre-reactor, reduce the load of electric heater simultaneously, increase the service life of electric heater; Reduce power consumption, thereby reduced the processing charges of product.
Description of drawings
Accompanying drawing is the utility model structural representation;
Among the figure: 1. pre-reactor, 2. unstripped gas superheater, 3. inlet pipeline, 4. hotline heater, 5. control valve.
The specific embodiment
For technological means, creation characteristic that the utility model is realized, reach purpose and be easy to understand understanding with effect, below in conjunction with concrete diagram, further set forth the utility model.
Shown in accompanying drawing; The auxiliary heater of pre-reactor comprises the auxiliary heater body in a kind of low temperature hydrogenation system benzene process, it is characterized in that; Said auxiliary heater body is arranged on the inlet pipeline 3 of said pre-reactor 1; In the present embodiment, said auxiliary heater body is arranged on pre-reactor 1 inlet pipeline 3 after the unstripped gas superheater 2, and said auxiliary heater body comprises hotline heater 4; Said hotline heater 4 is provided with the adjusting device that is used to regulate the conduction oil flow, and this adjusting device comprises control valve 5.
In the present embodiment, the concrete technical data of the hotline heater 4 of employing is:
Specification: Φ 600 * 4540 F=54.8m 2
Operating pressure: shell side 0.6Mpa tube side 3.03 Mpa
Operating temperature: 150/200 ℃ of 260/220 ℃ of tube side of shell side
Heat exchanger tube specification Φ 25 * 2 quantity: 247
The utility model is not limited to the above-mentioned specific embodiment, and all are based on the technical conceive of the utility model, and the structural improvement of having done all falls among the protection domain of the utility model.
The auxiliary heater of pre-reactor in a kind of low temperature hydrogenation system benzene process; Comprise the auxiliary heater body; Said auxiliary heater body is arranged on the inlet pipeline of said pre-reactor, and said auxiliary heater body comprises the hotline heater that is provided with control valve.The utility model is simple in structure, and is easy to adjust reliable, can satisfy the heat demand of each time period of pre-reactor, reduced the load of electric heater simultaneously, increased the service life of electric heater, reduced power consumption, thereby reduced the processing charges of product.

Claims (3)

1. the auxiliary heater of pre-reactor in the low temperature hydrogenation system benzene process comprises the auxiliary heater body, and it is characterized in that: said auxiliary heater body is arranged on the inlet pipeline of said pre-reactor.
2. the auxiliary heater of pre-reactor in a kind of low temperature hydrogenation system benzene process according to claim 1, it is characterized in that: said auxiliary heater body comprises hotline heater.
3. the auxiliary heater of pre-reactor in a kind of low temperature hydrogenation system benzene process according to claim 2, it is characterized in that: said hotline heater is provided with the control valve that is used to regulate the conduction oil flow.
CN2011203044200U 2011-08-19 2011-08-19 Auxiliary heater of pre-reactor in low-temperature hydrogenation and benzene-production process Expired - Lifetime CN202238019U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011203044200U CN202238019U (en) 2011-08-19 2011-08-19 Auxiliary heater of pre-reactor in low-temperature hydrogenation and benzene-production process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011203044200U CN202238019U (en) 2011-08-19 2011-08-19 Auxiliary heater of pre-reactor in low-temperature hydrogenation and benzene-production process

Publications (1)

Publication Number Publication Date
CN202238019U true CN202238019U (en) 2012-05-30

Family

ID=46099324

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011203044200U Expired - Lifetime CN202238019U (en) 2011-08-19 2011-08-19 Auxiliary heater of pre-reactor in low-temperature hydrogenation and benzene-production process

Country Status (1)

Country Link
CN (1) CN202238019U (en)

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Granted publication date: 20120530