JO3694B1 - نظام تقطير متعدد المراحل، وطريقة لتشغيله - Google Patents

نظام تقطير متعدد المراحل، وطريقة لتشغيله

Info

Publication number
JO3694B1
JO3694B1 JOP/2016/0024A JOP20160024A JO3694B1 JO 3694 B1 JO3694 B1 JO 3694B1 JO P20160024 A JOP20160024 A JO P20160024A JO 3694 B1 JO3694 B1 JO 3694B1
Authority
JO
Jordan
Prior art keywords
condenser
evaporator
pressure
vapor chamber
outlet
Prior art date
Application number
JOP/2016/0024A
Other languages
English (en)
Inventor
Markus Lehmann
Original Assignee
Tptec
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 Tptec filed Critical Tptec
Application granted granted Critical
Publication of JO3694B1 publication Critical patent/JO3694B1/ar

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/0082—Regulation; Control
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/26—Multiple-effect evaporating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0033—Other features
    • B01D5/0036—Multiple-effect condensation; Fractional condensation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0033—Other features
    • B01D5/0051—Regulation processes; Control systems, e.g. valves
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
    • B01D5/006—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with evaporation or distillation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/048—Purification of waste water by evaporation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/08—Seawater, e.g. for desalination
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00—Apparatus for treatment of water, waste water or sewage
    • C02F2201/009—Apparatus with independent power supply, e.g. solar cells, windpower, fuel cells
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/42—Liquid level
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124—Water desalination
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20—Controlling water pollution; Waste water treatment
    • Y02A20/208—Off-grid powered water treatment
    • Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Automation & Control Theory (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

<strong>يتعلق الاختراع الحالي بنظام تقطير متعدد المراحل (1) يحتوي على المراحل (</strong><span dir="LTR">Si</span><strong>)، حيث </strong><span dir="LTR">i</span><strong> = 1، ... </strong><span dir="LTR">n</span><strong>، حيث تعمل كل مرحلة (</strong><span dir="LTR">Si</span><strong>) في مدى من الضغط ودرجة الحرارة (</strong><span dir="LTR">Pi</span><strong>، </strong><span dir="LTR">Ti</span><strong>) أعلى من المرحلة (</strong><span dir="LTR">Si</span><strong>)</strong> <strong>التي تليها (</strong><span dir="LTR">Si+1</span><strong>) أثناء تشغيل نظام التقطير. حيث تتكون كل مرحلة (</strong><span dir="LTR">Ci</span><strong>) من مبخر (</strong><span dir="LTR">Ei</span><strong>) ومكثف (</strong><span dir="LTR">Ci</span><strong>)، ويحتوي كل مبخر (</strong><span dir="LTR">Ei</span><strong>) وكل مكثف (</strong><span dir="LTR">Ci</span><strong>) على قناة محكمة الضغط (2) متصلة بغرفة بخار (6)، وتكون غرفة البخار (6) من كل مبخر (</strong><span dir="LTR">Ei</span><strong>) على اتصال بواسطة الضغط بغرفة البخار (6) التي توجد في المكثف (</strong><span dir="LTR">Ci</span><strong>) من نفس المرحلة (</strong><span dir="LTR">Si</span><strong>) عن طريق أنبوب بخار محكم الضغط (7) ذو مقطع عرضي كبير. ويتصل كل مخرج (5) من كل مبخر (</strong><span dir="LTR">Ei</span><strong>) بمدخل الرذاذ (3) من المبخر التالي (</strong><span dir="LTR">Ei+1</span><strong>)، ويتصل المخرج (5) من المبخر الأخير (</strong><span dir="LTR">En</span><strong>) بمدخل الرذاذ (3) من المبخر الأول (</strong><span dir="LTR">E1</span><strong>) عن طريق قناة السوائل (8) وذلك لتشكيل دائرة المبخر. ويتصل كل مخرج (5) من كل مكثف (</strong><span dir="LTR">Ci</span><strong>) بمدخل الرذاذ (3) من المكثف السابق (</strong><span dir="LTR">Ci-1</span><strong>)، ويتصل المخرج (5) من المكثف الأول (</strong><span dir="LTR">C1</span><strong>) بمدخل الرذاذ (3) في المكثف الأخير (</strong><span dir="LTR">Cn</span><strong>) عن طريق قناة السوائل (9) وذلك لتشكيل دائرة المكثف. ووفقا للاختراع، يجب أن يوصل أنبوب بخار (10) واحد على الأقل ذو طرف أول بإحدى قنوات السوائل (9) بين المكثفات (</strong><span dir="LTR">Ci+1</span><strong>) و (</strong><span dir="LTR">Ci</span><strong>) أو يوصل بقناة السوائل (8) بين المبخرات (</strong><span dir="LTR">En</span><strong>) و (</strong><span dir="LTR">E1</span><strong>)، ويوصل الطرف الثاني من الأنبوب بغرفة البخار، ويكون ضغطه (</strong><span dir="LTR">P</span><strong>) أثناء تشغيل نظام التقطير أعلى من الضغط (</strong><span dir="LTR">Pi</span><strong>) في غرفة البخار (6) التي توجد في المكثف (</strong><span dir="LTR">Ci</span><strong>) وأعلى من الضغط (</strong><span dir="LTR">Pi</span><strong>) في غرفة البخار (6) التي توجد في المبخر (</strong><span dir="LTR">E1</span><strong>). ويتعلق الاختراع الحالي أيضا بطريقة لتنفيذ عملية التقطير من خلال الاستفادة من نظام مبتكر، فضلا عن وحدة تحكم بهذا النظام.</strong>
JOP/2016/0024A 2015-02-13 2016-02-11 نظام تقطير متعدد المراحل، وطريقة لتشغيله JO3694B1 (ar)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH00198/15A CH710735A1 (de) 2015-02-13 2015-02-13 Mehrstufige Destillationsanlage, Verfahren zum Betreiben einer solchen und Steuerung dafür.

Publications (1)

Publication Number Publication Date
JO3694B1 true JO3694B1 (ar) 2020-08-27

Family

ID=52484293

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (18)

Country Link
US (1) US10427066B2 (ar)
EP (1) EP3256229B1 (ar)
JP (1) JP6744868B2 (ar)
KR (1) KR102503071B1 (ar)
CN (1) CN107405532B (ar)
AU (1) AU2016217954B2 (ar)
BR (1) BR112017017382B1 (ar)
CH (1) CH710735A1 (ar)
ES (1) ES2734258T3 (ar)
HK (1) HK1243372B (ar)
HU (1) HUE045101T2 (ar)
IL (1) IL253908B (ar)
JO (1) JO3694B1 (ar)
MA (1) MA41491B1 (ar)
RU (1) RU2690922C2 (ar)
SG (1) SG11201706435YA (ar)
TR (1) TR201909948T4 (ar)
WO (1) WO2016128455A1 (ar)

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CN109336324B (zh) * 2018-11-24 2023-09-12 无锡诚尔鑫环保装备科技有限公司 一种反渗透浓水制取纯水装置及其工作方法
CN110876856B (zh) * 2019-12-11 2021-12-07 宜宾丝丽雅股份有限公司 一种粘胶纤维生产中二硫化碳的冷凝回收方法及系统
CN114806718B (zh) * 2022-04-06 2023-06-23 德帕姆(杭州)泵业科技有限公司 一种玫瑰精油萃取装置
CN116554967A (zh) * 2023-06-29 2023-08-08 浙江茶博士生物科技有限公司 一种利用阶梯式压差从茶叶中萃取精油的设备和方法

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB381439A (en) * 1931-07-15 1932-10-06 Metallgesellschaft Ag Process of and apparatus for the separation of solid substances from liquids by vacuum cooling in stages
GB939188A (en) * 1961-05-13 1963-10-09 Nirex Ingenior Aktieselskab Improvements in and relating to a vacuum distillation plant for the production of fresh water from sea water onboard ships
US3206379A (en) * 1962-05-31 1965-09-14 Robert H Hill Multi-stage convective distillation system
US3249517A (en) * 1963-04-12 1966-05-03 Lockman Carl Johan Apparatus for multi stage flash evaporation
US3583895A (en) * 1969-05-20 1971-06-08 Donald F Othmer Evaporation using vapor-reheat and multieffects
BE754341A (fr) * 1969-08-04 1971-01-18 Hydro Chem & Mineral Corp Appareil de condensation multi-etage
US3856631A (en) * 1970-03-16 1974-12-24 Sigworth H Process and apparatus for separating water from non-volatile solutes
EP1385592A1 (de) * 2001-05-02 2004-02-04 Peter Dr.-Ing. Vinz Ausdampfverfahren zur herstellung von reinem trinkwasser und hochprozentiger sole aus salzhaltigen rohwässern
BRPI0719253A2 (pt) * 2006-10-10 2014-01-28 Texas A & M Univ Sys Sistema de dessalinização
EP2139571A1 (de) * 2007-04-04 2010-01-06 Lehmann, Markus Verfahren zum destillieren eines ausgangsmaterials und anlage zum durchführen eines solchen verfahrens
WO2008122137A1 (de) 2007-04-04 2008-10-16 Markus Lehmann Verfahren zum trocknen eines nassmaterials
US8505323B2 (en) * 2007-06-07 2013-08-13 Deka Products Limited Partnership Water vapor distillation apparatus, method and system
GR20110100052A (el) * 2011-02-02 2012-09-20 Αριστειδης Εμμανουηλ Δερμιτζακης Πολυβαθμια αφαλατωση χαμηλης ενθαλπιας
CN204073478U (zh) * 2014-08-15 2015-01-07 青岛天雄健工贸有限公司 一种多级分子蒸馏设备

Also Published As

Publication number Publication date
EP3256229B1 (de) 2019-04-10
JP2018505052A (ja) 2018-02-22
HUE045101T2 (hu) 2019-12-30
US10427066B2 (en) 2019-10-01
RU2017131841A3 (ar) 2019-03-28
HK1243372B (zh) 2020-03-20
BR112017017382A2 (pt) 2018-04-03
WO2016128455A1 (de) 2016-08-18
KR102503071B1 (ko) 2023-02-22
TR201909948T4 (tr) 2019-07-22
US20180021691A1 (en) 2018-01-25
AU2016217954A1 (en) 2017-09-14
SG11201706435YA (en) 2017-09-28
CN107405532A (zh) 2017-11-28
ES2734258T3 (es) 2019-12-05
CN107405532B (zh) 2019-11-26
KR20170118128A (ko) 2017-10-24
JP6744868B2 (ja) 2020-08-19
IL253908B (en) 2021-01-31
MA41491A (fr) 2017-12-20
RU2690922C2 (ru) 2019-06-06
IL253908A0 (en) 2017-10-31
MA41491B1 (fr) 2019-08-30
RU2017131841A (ru) 2019-03-13
EP3256229A1 (de) 2017-12-20
AU2016217954B2 (en) 2019-11-07
BR112017017382B1 (pt) 2021-05-25
CH710735A1 (de) 2016-08-15

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