CN103316495A - Alcohol recovery system adopting waste heat to heat - Google Patents

Alcohol recovery system adopting waste heat to heat Download PDF

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Publication number
CN103316495A
CN103316495A CN2012100784679A CN201210078467A CN103316495A CN 103316495 A CN103316495 A CN 103316495A CN 2012100784679 A CN2012100784679 A CN 2012100784679A CN 201210078467 A CN201210078467 A CN 201210078467A CN 103316495 A CN103316495 A CN 103316495A
Authority
CN
China
Prior art keywords
condenser
tower
waste heat
heat
alcohol
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.)
Pending
Application number
CN2012100784679A
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Chinese (zh)
Inventor
周伯雅
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.)
XINGHUA GREEN BIOLOGICAL PREPARATION CO Ltd
Original Assignee
XINGHUA GREEN BIOLOGICAL PREPARATION 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 XINGHUA GREEN BIOLOGICAL PREPARATION CO Ltd filed Critical XINGHUA GREEN BIOLOGICAL PREPARATION CO Ltd
Priority to CN2012100784679A priority Critical patent/CN103316495A/en
Publication of CN103316495A publication Critical patent/CN103316495A/en
Pending legal-status Critical Current

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

The present invention discloses an alcohol recovery system adopting waste heat to heat. The system comprises an alcohol recovery tower and a waste heat heater, wherein the alcohol recovery tower comprises a tower kettle, a tower body, a condenser and a storage tank, the tower kettle is connected with one end of the condenser through the tower body, the other end of the condenser is connected with the storage tank, the waste heat heater is a heat exchanger, a cold fluid outlet of the waste heat heater is communicated with the tower kettle of the alcohol recovery tower, and a hot fluid inlet is connected with a cold fluid outlet of the condenser. The alcohol recovery system has characteristics of energy source saving and high recovery efficiency.

Description

A kind of alcohol recovery system of waste-heat
Technical field
The present invention relates to a kind of alcohol recovery system, be specifically related to the alcohol recovery system that a kind of heat that utilizes condensation alcohol to produce carries out the charging heating.
Background technology
Need to alcohol be reclaimed in industries such as pharmacy, food, light industry, chemical industry, at present alcohol distillation column is adopted in the recovery of alcohol more, the Diluted Alcohol solution that need are reclaimed carries out heated volatile, after tower body rectifying, improve the concentration of alcoholic solution, reach the purpose of recovered alcohol.The heat that the alcohol condensation produces does not take full advantage of, and has wasted energy.
Summary of the invention
To the objective of the invention is the defective that exists in the prior art in order solving, a kind of alcohol recovery system of energy savings to be provided.
In order to achieve the above object, the invention provides a kind of alcohol recovery system of waste-heat, comprise alcohol distillation column and heater heated by waste heat; Alcohol distillation column comprises tower reactor, body of the tower, condenser and basin; Tower reactor links to each other with described condenser one end by body of the tower; The condenser other end links to each other with described basin; Heater heated by waste heat is heat exchanger, and its cold fluid outlet is connected with the tower reactor of described alcohol distillation column, and the hot fluid entrance links to each other with the cold fluid outlet of described condenser.
Alcohol recovery system of the present invention has the following advantages compared to existing technology: utilize the heat of the formation after the cold fluid heat exchange in the condenser of alcohol distillation column, raw material is carried out heat exchange, take full advantage of energy, improved organic efficiency.
Description of drawings
Fig. 1 is the structural representation of alcohol recovery system of the present invention.
Among the figure, 1-tower reactor, 2-body of the tower, 3-condenser, the cold fluid entrance of 31-condenser, the cold fluid outlet of 32-condenser, 4-basin, 5-heater heated by waste heat, 51-hot fluid entrance, the outlet of 52-hot fluid, 6-feed(raw material)inlet.
The specific embodiment
The present invention is described in detail below in conjunction with the specific embodiment.
Referring to Fig. 1, alcohol recovery system of the present invention comprises alcohol distillation column and heater heated by waste heat 5.Alcohol distillation column comprises tower reactor 1, body of the tower 2, condenser 3 and basin 4.Condenser 3 one ends link to each other with tower reactor by body of the tower 2, and the other end links to each other with basin 4.Heater heated by waste heat 5 is heat exchanger.The cold fluid of condenser outlet 32 links to each other with the hot fluid entrance 51 of heater heated by waste heat 5.The cold fluid outlet of heater heated by waste heat 5 links to each other with tower reactor 1.
When alcohol is reclaimed, first alcohol is passed through heater heated by waste heat 5, enter in the tower reactor 1, heated volatile in tower reactor passes in the basin 4 by condenser 3.When alcohol continues to pass into heater heated by waste heat 5, condensed water from the condensing water inlet 31 of condenser enter in the condenser with the alcohol steam heat exchange after, enter the heater heated by waste heat 5 from the cold fluid of the condenser outlet 32 hot fluid entrances 51 by heater heated by waste heat 5 and to carry out heat exchange with raw material alcohol, cold water is directly discharged from the hot fluid outlet 52 of heater heated by waste heat 5.(being the cold fluid entrance) enters the heater heated by waste heat 5 after the heat exchange raw material alcohol from feed(raw material)inlet 6, passes into tower reactor 1 interior continuation heated volatile from the cold fluid outlet of heater heated by waste heat 5, is recovered in the basin 4 by condenser 3.

Claims (1)

1. the alcohol recovery system of a waste-heat is characterized in that: comprise alcohol distillation column and heater heated by waste heat; Described alcohol distillation column comprises tower reactor, body of the tower, condenser and basin; Described tower reactor links to each other with described condenser one end by body of the tower; The described condenser other end links to each other with described basin; Described heater heated by waste heat is heat exchanger; The cold fluid outlet of described heater heated by waste heat is connected with the tower reactor of described alcohol distillation column, and the hot fluid entrance links to each other with the cold fluid outlet of described condenser.
CN2012100784679A 2012-03-20 2012-03-20 Alcohol recovery system adopting waste heat to heat Pending CN103316495A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012100784679A CN103316495A (en) 2012-03-20 2012-03-20 Alcohol recovery system adopting waste heat to heat

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012100784679A CN103316495A (en) 2012-03-20 2012-03-20 Alcohol recovery system adopting waste heat to heat

Publications (1)

Publication Number Publication Date
CN103316495A true CN103316495A (en) 2013-09-25

Family

ID=49185711

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2012100784679A Pending CN103316495A (en) 2012-03-20 2012-03-20 Alcohol recovery system adopting waste heat to heat

Country Status (1)

Country Link
CN (1) CN103316495A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104241170A (en) * 2014-07-24 2014-12-24 如皋市易达电子有限责任公司 Alcohol recycling condensation system for ultrasonic cleaning
CN107261530A (en) * 2017-07-05 2017-10-20 临沂市金沂蒙生物科技有限公司 Alcohol circulating and evaporating system in acetaldehyde production

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104241170A (en) * 2014-07-24 2014-12-24 如皋市易达电子有限责任公司 Alcohol recycling condensation system for ultrasonic cleaning
CN104241170B (en) * 2014-07-24 2017-08-11 如皋市易达电子有限责任公司 A kind of ultrasound utilizes condenser system with alcohol recycle
CN107261530A (en) * 2017-07-05 2017-10-20 临沂市金沂蒙生物科技有限公司 Alcohol circulating and evaporating system in acetaldehyde production

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C06 Publication
PB01 Publication
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20130925