JPS59222202A - 分留塔と協働するオ−バ−ヘツド蓄積器から引かれるオ−バ−ヘツド液体生成物の流れに望みのａｓｔｍ終点温度を維持する方法と装置 - Google Patents
分留塔と協働するオ−バ−ヘツド蓄積器から引かれるオ−バ−ヘツド液体生成物の流れに望みのａｓｔｍ終点温度を維持する方法と装置Info
- Publication number
- JPS59222202A JPS59222202A JP59089191A JP8919184A JPS59222202A JP S59222202 A JPS59222202 A JP S59222202A JP 59089191 A JP59089191 A JP 59089191A JP 8919184 A JP8919184 A JP 8919184A JP S59222202 A JPS59222202 A JP S59222202A
- Authority
- JP
- Japan
- Prior art keywords
- signal
- overhead
- time
- determining
- actual
- 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.)
- Granted
Links
- 239000012263 liquid product Substances 0.000 title claims description 53
- 238000000034 method Methods 0.000 title claims description 47
- 238000004821 distillation Methods 0.000 title description 4
- 238000005194 fractionation Methods 0.000 claims description 40
- 238000009835 boiling Methods 0.000 claims description 35
- 238000010992 reflux Methods 0.000 claims description 21
- 239000000047 product Substances 0.000 claims description 17
- 230000004044 response Effects 0.000 claims description 16
- 238000007701 flash-distillation Methods 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 230000008859 change Effects 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 4
- 238000004508 fractional distillation Methods 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims 3
- 238000013021 overheating Methods 0.000 claims 1
- 230000008569 process Effects 0.000 description 29
- 238000004364 calculation method Methods 0.000 description 24
- 239000010779 crude oil Substances 0.000 description 10
- 239000012530 fluid Substances 0.000 description 10
- 229930195733 hydrocarbon Natural products 0.000 description 9
- 150000002430 hydrocarbons Chemical class 0.000 description 9
- 238000005259 measurement Methods 0.000 description 8
- 239000004215 Carbon black (E152) Substances 0.000 description 7
- 238000004458 analytical method Methods 0.000 description 7
- 238000000926 separation method Methods 0.000 description 6
- 238000012937 correction Methods 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000009466 transformation Effects 0.000 description 3
- 238000009529 body temperature measurement Methods 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 238000000611 regression analysis Methods 0.000 description 2
- 230000011664 signaling Effects 0.000 description 2
- 238000000844 transformation Methods 0.000 description 2
- 235000021028 berry Nutrition 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 231100000817 safety factor Toxicity 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000013519 translation Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/42—Regulation; Control
- B01D3/4211—Regulation; Control of columns
- B01D3/4238—Head-, side- and bottom stream
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S203/00—Distillation: processes, separatory
- Y10S203/19—Sidestream
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US498997 | 1983-05-27 | ||
| US06/498,997 US4558423A (en) | 1983-05-27 | 1983-05-27 | Utilization of an ASTM end point temperature for controlling a fractional distillation process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59222202A true JPS59222202A (ja) | 1984-12-13 |
| JPS6320164B2 JPS6320164B2 (enExample) | 1988-04-26 |
Family
ID=23983366
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59089191A Granted JPS59222202A (ja) | 1983-05-27 | 1984-05-02 | 分留塔と協働するオ−バ−ヘツド蓄積器から引かれるオ−バ−ヘツド液体生成物の流れに望みのａｓｔｍ終点温度を維持する方法と装置 |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US4558423A (enExample) |
| EP (1) | EP0130352A3 (enExample) |
| JP (1) | JPS59222202A (enExample) |
| BR (1) | BR8402075A (enExample) |
| CA (1) | CA1204073A (enExample) |
| ES (1) | ES532830A0 (enExample) |
| NO (1) | NO842105L (enExample) |
| ZA (1) | ZA842802B (enExample) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3680636D1 (de) * | 1985-05-03 | 1991-09-05 | Foxboro Co | Regelung des trennungspunktes bei der destillation. |
| US5132918A (en) * | 1990-02-28 | 1992-07-21 | Funk Gary L | Method for control of a distillation process |
| US5396416A (en) * | 1992-08-19 | 1995-03-07 | Continental Controls, Inc. | Multivariable process control method and apparatus |
| US5663492A (en) * | 1996-06-05 | 1997-09-02 | Alapati; Rama Rao | System for continuous analysis and modification of characteristics of a liquid hydrocarbon stream |
| EP1210405A4 (en) * | 1999-06-18 | 2003-04-23 | Advanced Res & Tech Inst | CARDIOMYOCYTES WITH ENHANCED PROLIFERATION POTENTIAL, THEIR OBTAINMENT AND THEIR USE |
| US6869501B2 (en) | 2001-12-20 | 2005-03-22 | 3M Innovative Properties Company | Continuous process for controlled concentration of colloidal solutions |
| US20030116290A1 (en) * | 2001-12-20 | 2003-06-26 | 3M Innovative Properties Company | Continuous process for controlled evaporation of black liquor |
| US20080275653A1 (en) * | 2005-09-14 | 2008-11-06 | Symyx Technologies, Inc. | Microscale Flash Separation of Fluid Mixtures |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3405035A (en) * | 1967-10-23 | 1968-10-08 | Universal Oil Prod Co | Fractionator system with side stream product removal and internal reflux control |
| US3619377A (en) * | 1969-08-04 | 1971-11-09 | Phillips Petroleum Co | Control of composition of overhead vaporous product in a partially condensing fractionation column |
| US3907388A (en) * | 1970-08-13 | 1975-09-23 | Shell Oil Co | Method for blending multiple component streams using loss-in-weight boiling point analysis |
| US3911259A (en) * | 1974-04-11 | 1975-10-07 | Texaco Inc | Means for controlling the reflux rate and the reboiler temperature of a tower |
| FR2272707B1 (fr) * | 1974-05-30 | 1977-03-11 | Elf Aquitaine | Procede de commande d'une colonne de distillation atmospherique de petrole brut |
| US3996785A (en) * | 1975-12-29 | 1976-12-14 | Texaco Inc. | Means for on-line determination of boiling point properties of crude oil |
| US4166770A (en) * | 1978-05-22 | 1979-09-04 | Phillips Petroleum Company | Fractionation control |
| US4295196A (en) * | 1980-07-02 | 1981-10-13 | Phillips Petroleum Company | Fractional distillation column control |
| US4347577A (en) * | 1980-12-15 | 1982-08-31 | Texaco Inc. | Feedstock temperature control system |
-
1983
- 1983-05-27 US US06/498,997 patent/US4558423A/en not_active Expired - Fee Related
-
1984
- 1984-04-13 ZA ZA842802A patent/ZA842802B/xx unknown
- 1984-05-02 JP JP59089191A patent/JPS59222202A/ja active Granted
- 1984-05-03 BR BR8402075A patent/BR8402075A/pt unknown
- 1984-05-16 CA CA000454505A patent/CA1204073A/en not_active Expired
- 1984-05-25 EP EP84105968A patent/EP0130352A3/en not_active Withdrawn
- 1984-05-25 NO NO842105A patent/NO842105L/no unknown
- 1984-05-25 ES ES532830A patent/ES532830A0/es active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| ES8503962A1 (es) | 1985-04-01 |
| JPS6320164B2 (enExample) | 1988-04-26 |
| BR8402075A (pt) | 1985-03-26 |
| NO842105L (no) | 1984-11-28 |
| EP0130352A3 (en) | 1986-12-30 |
| US4558423A (en) | 1985-12-10 |
| EP0130352A2 (en) | 1985-01-09 |
| ZA842802B (en) | 1984-11-28 |
| ES532830A0 (es) | 1985-04-01 |
| CA1204073A (en) | 1986-05-06 |
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