EP0063141A1 - Dispositif de distillation ameliore - Google Patents

Dispositif de distillation ameliore

Info

Publication number
EP0063141A1
EP0063141A1 EP81902919A EP81902919A EP0063141A1 EP 0063141 A1 EP0063141 A1 EP 0063141A1 EP 81902919 A EP81902919 A EP 81902919A EP 81902919 A EP81902919 A EP 81902919A EP 0063141 A1 EP0063141 A1 EP 0063141A1
Authority
EP
European Patent Office
Prior art keywords
tube
wobbling
fluid
tubes
transfer tubes
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.)
Withdrawn
Application number
EP81902919A
Other languages
German (de)
English (en)
Other versions
EP0063141A4 (fr
Inventor
Yao Tzu Dr. Li
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of EP0063141A1 publication Critical patent/EP0063141A1/fr
Publication of EP0063141A4 publication Critical patent/EP0063141A4/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/22—Evaporating by bringing a thin layer of the liquid into contact with a heated surface
    • B01D1/222—In rotating vessels; vessels with movable parts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/06—Evaporators with vertical tubes
    • B01D1/065—Evaporators with vertical tubes by film evaporating
    • 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
    • B01D3/006—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping by vibration
    • 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
    • B01D3/04—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping pipe stills
    • 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
    • C02F1/08—Thin film evaporation

Definitions

  • This invention is an improvement over the existing art for the evaporation or distillation of fluids. It may be used for concentration by removing part of the liquid (as in orange juice), for desalination by condensing the water vapor, or for distillation by separating the various ingredients in the fluid (as in alcohol and water). In all these applications the evaporation (or condensation) of the fluid occurs primarily at the interface between the liquid and its vapor while the needed energy is transmitted from a heat source through the container wall to the liquid and then through the liquid to the interface to support the evaporation.
  • a further object is to lower the heat resistance of the fluid being evaporated and reduce temperature differentials.
  • a further object is to supply the energy needed to evaporate the fluid by the condensation of the evaporated vapor.
  • a further object is to supply the energy needed to evaporate the fluid by the condensation of the evaporated vapor.
  • Novel distillation apparatus comprises pairs of wobbling thin-walled tubes to evaporate the fluid flowing inside the wobbling tubes with the heat energy supplied by condensing the stream of vapor which surrounds the outside surface of the tubes.
  • the condensates that form droplets outside the tubes will be thrown off by the wobbling motion and splashed between the tubes to activate further condensation.
  • the wobbling motion of the tube similar to the circular motion of tea inside a wobbling tea cup, effectively reduces the temperature difference between the vapor outside the tubes and the vapor inside the tubes. Consequently less energy or less equipment is needed for a given task than with conventional equipment. Vapor and fluid interconnections appropriate to the desired distillation system are provided.
  • Fig. 1 is an end plan view of a wobbling evaporator
  • Fig. 2 is an elevation view, with cut out sections, of a wobbling evaporator
  • Fig. 3 is an end plan view of two concentric wobbling evaporators to achieve dynamic balancing.
  • Fig. 4 is a schematic diagram of two pairs of wobbling systems to achieve dynamic balancing
  • Fig. 5 is an elevation schematic view of cascading wobbling evaporators to be used as desalination system
  • Fig. 6 is an elevation view, with cut out sections, of a vapor compression wobbling drive desalination system
  • Fig. 7 is a schematic elevation view of a distillation system
  • Fig. 8 is an elevation schematic view ⁇ f two wobbling systems used as a distillation system
  • Fig. 9 is a perspective view of a disc-shaped spray head
  • Fig. 10 is an end view of a distillation system incorporating pairs of heat transfer tubes
  • Fig. 11 is a cross section view of distillation apparatus incorporating pairs of heat transfer tubes
  • Fig. 12 is a schematic end view of a fluid distribution system for the apparatus of Figs. 10 and 11,
  • Fig. 13 shows schematically further details concerning the apparatus of Fig. 12,
  • Fig. 14 is a schematic end view of apparatus for use with high viscosity fluids
  • Fig. 15 is an elevation view of the apparatus of Fig. 14,
  • Fig. 16 is an end view of another fluid distribution system
  • Fig. 17 is an elevation view of the system of Fig. 16,
  • Fig. 18 is a schematic diagram showing details of one configuration of convoluted membrane
  • Fig. 19 shows schematically details of another convoluted membrane configuration
  • Fig. 20 shows a schematic diagram of a universal joint connecting the frame and a wobbling member. Description Of Preferred Embodiments
  • Figure 1 shows the end view of a generalized wobbling evaporator which consists of an outer shell 1 and a wobbling container 2.
  • Three heat transfer tubes 7 are shown to perform the evaporation and condensation operation. In actual construction several dozens of tubes may be installed in one container.
  • Three brackets 24 are attached to the ends of the container 2.
  • Three cranks 51 together with three sets of shafts 21 and 23 bearings 22 and 24 are used to guide the container 2 to revolve in the wobbling motion.
  • a motor (not shown) may be used to drive any one of the three shafts 21 to wobble the container 2 as shown in the drawing container 2 is pivoted to arms 51 connected to shafts 21.
  • the pivot points 23 on container 2 travel through circles defined by the arms 51. The rotation of the points 23 through these small circles causes the container 2 to perform a wobbling motion.
  • fluid to be evaporated is represented by arrow 101 which flows into tube 18 which revolves in bushing 19.
  • the center of bushing 19 is also the center of wobbling for tube 7.
  • the wobbling motion of tube 7 will drive the "L" shaped pipe 18 to revolve in the bushing 19 and discharge the fluid from the head 20 at the far side of the tube 7 from the wobbling center.
  • the fluid discharge from head 20 becomes fluid stream 6 which revolves inside tube 7 and discharges into chamber 3' and then flows out through pipe 17 as represented by arrow 102.
  • Tube 7 wobbles but does not revolve.
  • the revolving stream 6 coats the inside surface of tube 7 with a thin film 5 which readily evaporates into vapor and escapes from the two ends of tube 7.
  • the upper ends of tube 7 connect to chamber 3 and exit through opening 26 as arrow 103.
  • the lower end of tube 7 opens to chamber 3' and exits through opening 27 as arrow 104.
  • Chambers 3 and 3' are separated by flexible barrier 28.
  • arrow 103 and arrow 104 nay be arranged to have one flowing inward while the other is flowing outward to achieve continuous circulation and to help the evaporation.
  • the flexible barrier 28 is omitted so that only one exit. is sufficient to bring the vapor out. The detailed arrangement of specific applications is discussed below.
  • High temperature vapor 111 will be introduced from inlet pipe 10 through flexible coupling 9 and pipe 8 into the inside chamber 4 of container 3. In contact with the coupler tube 7 the vapor will condense into droplets 25 which splashes inside chamber 4 against the outside surface of tubes 7 and thereby increases the condensation rate. Finally, the condensation will be collected near the bottom edge of chamber 4 and discharged through pipe 11, flexible coupling 12 and drain pipe 13 to become distillate 113.
  • a second vapor passage 14-15-16 with vapor 112 is shown at the lower end of the system. This double ended vapor passage arrangement is needed in the distillation system described later in conjunction with Figure 7 and is not essential for the desalination system described in conjunction with Figure 6.
  • the wobbling drive of Figures 1 and 2 exhibits a revolving centrifugal force of the center of mass with respect to its wobbling center.
  • Figure 3 shows one way to balance the revolving forces by having two sets of concentric wobbling systems with the two mass centers 31 and 32 opposite to each other with respect to their common wobbling center 30.
  • 31 is the mass center of the inner system 33 which is guided by three cranks 51, 52 and 53.
  • 32 is the mass center of the outer system 34 and is guided by three cranks 54, 55 and 56. Both systems have the same wobbling center 30.
  • Two gears 58 and 59 coupled by chain 57 are used to maintain the proper orientation of the two systems.
  • Figure 4 shows schematically an arrangement wherein two pairs of wobbling systems are coupled together to achieve dynamic balancing.
  • the four wobbling systems are symmetrical with each other and of the same mass.
  • mass centers 60, 61, 62 and 63 are shown to revolve with respect to the respective wobbling centers 64, 65, 66 and 67 and with orientation to provide dynamic balancing.
  • Figure 5 shows the operation of a desalination system where vapor is to be evaporated from sea water and recondensed to get distilled water.
  • Heat energy is provided by a boiler 80 where high temperature steam 92 is generated from feed water 91.
  • This high temperature steam is blended with low temperature vapor 303 to form vapor 111 which is to be condensed in a wobbling evaporator 81 which operates on the same principle as that shown in Figure 2 but is here shown schematically.
  • the condensate 113 of vapor 111 is channelled as part of of the desired output.
  • Sea water 101 is admitted to the wobbling evaporator 81 to generate vapor 103. Excessive sea water is flushed out at 102. Heat exchanger arrangements as represented by 115, 215 and 315 are used to recover some of the heat energy in the condensate 113, 114 and 115 and exit flow 102, 202 and 302. Arrows 105, 205 and 305 are used to indicate that in some applications reflux of the sea water may be advisable to achieve higher operation efficiency.
  • Vapor 103 is directed to a second wobbling evaporator 82 to become input vapor 211 and condensed as distillate water 213.
  • Sea water 201 is admitted to evaporator 82 in the same manner as sea water 101 is admitted to evaporator 81.
  • the same operation, as illustrated for evaporator 81, is thus repeated in evaporator 82 and likewise in evaporator 83, as shown in Figure 5.
  • vapor 303 is cooler than vapor 311 which is cooler than vapor 211 and in turn cooler than vapor 111.
  • the total temperature drop across the series of evaporators is then rejuvenated by the boiler 80.
  • Fig. 5 The distillation organization of Fig. 5 would also work if the wobbling evaporators are replaced by conventional condensor-evaporators.
  • the wobbling evaporator provides a lower temperature gradient per stage than that in conventional condensor-evaporators. There will be a similar gradient between the temperature needed to evaporate sea water and the temperature to condense the same vapor to distilled water in either system. But in addition to this the temperature gradient needed to transfer the heat will be different. For this reason for a given temperature rise or energy input provided by the boiler 80, more stages of wobbling evaporators can be accommodated and therefore more output in distilled water will be produced than with conventional condensor-evaporators.
  • FIG. 6 shows a wobbling drive vapor compression evaporator where wobbling containers 2 and 2' are shown. These containers are driven to wobble by motor 31 through pinion 30, gear 29 and crank shaft 21 in the same way as in the apparatus of Figure 2.
  • Sea water 101 is distributed by piping system 36 to the various revolving pipes 18 to discharge into heat transfer tubes 7 . Inside tube 7 the sea water will evaporate as vapor 103 or 104 and collect into chamber 3.
  • a centrifugal compressor 33 driven by shaft 32 inside housing 34 will compress vapor 103 into vapor 111 which has a higher pressure and temperature than vapor 103.
  • Vapor 111 is distributed by conduit system 10 flexible coupling 9 and conduit 8 to the inside chamber 4 and 4' of container 2 and 2'. Vapor 111 will be cooled and condensed by tubes 7 with the heat of condensation transmitted through the wall of tube 7 to evaporate sea water inside tube 7 in the same manner as illustrated before for the apparatus of Figure 2.
  • the use of the wobbling drive system reduces the temperature gradient and the pressure gradient between the vapors across the heat transfer barriers. The net result is a reduction of the power needed to drive the centrifugal compressor 33 and therefore reduced operating cost of the plant.
  • Figure 7 illustrates the general concept of a distillation column for separating two ingredients I and II soluble with each other.
  • fluid film 5 flows downward and a vapor 50 flows upward inside tube 7.
  • the fluid film 5 will start with fluid input 101 at the top and become fluid output 102 at the bottom of the tube 7.
  • the consistency of fluid 101 is strong in ingredient I whereas the consistency of fluid 102 is strong in ingredient II. Both ingredients are mutually soluble like alcohol and water.
  • vapor 103 is strong in ingredient I and vapor 104 is strong in ingredient II.
  • Heat exchanger 37 is used to condense the vapor 103 to become fluid 101 whereas heat exchanger 38 is used to evaporate fluid 102 to become vapor 104 and thus close the loop.
  • Inlet 41 brings in fluid with intermediate consistency in ingredient I and II whereas outlet 39 extracts fluid strong in ingredient I and outlet 40 extracts fluid strong in ingredient II.
  • the wobbling evaporator 86 is essentially the same as the evaporator of Figure 2 with the exception that the flexible barrier 28 of Figure 2 is not needed.
  • the upper chamber 3 of evaporator 85 supplies vapor 103 which is condensed in chamber 4 of unit 86 to become fluid 101 which is pumped by pump 50 to return to unit 85 and be discharged through revolving tube 18 to coat the inside surface of tube 7.
  • This fluid will be re-evaporated as vapor to fill the chamber 50 and to ascend to chamber 3 to complete the loop. Part of the fluid will flow down the inside surface of tube 7 to reach the lower chamber 3'.
  • fluid 102 will be drained from tube 17 and moved by pump 51 to reach the revolving tube 18' of unit 86 to coat the inside surface of tube 7'.
  • the vapor thus generated will fill up chamber 50' and thus collect as vapor 104 to be transported back to chamber 3' of unit 85.
  • Part of the vapor will be condensed into the inside surface of tube 7 and flow down back to chamber 3' and part of the vapor will ascend to chamber 3.
  • Inlet 41 represents an influx of a fluid with intermediate consistency in ingredients I and II.
  • Spray head 43 represents a disc shaped spray head to distribute the fluid evenly to the inside surface of tube 7.
  • Disc shaped spray head 43 and the disc shaped spray 43' as shown in Figure 9 may be used as an alternate to the revolving tube 18 for distributing the fluid.
  • Tube 18 discharges fluid at the head of the revolving stream 6 of Figure 2. In so doing it minimizes splashes and thereby avoids the mixing of the salt water mists with the clean vapor.
  • the spray head 43 used at the middle of the tube offers a simpler mechanical configuration where the mist forming is not objectionable.
  • Pipes 39 and 40 represent the outlets of the fluids which are rich in ingredients I and II respectively.
  • Pump 52 and the associated pipe-line represent the auxiliary circulation loop of the fluid to be evaporated.
  • An auxiliary fan or a pressurized fan may be needed to circulate the vapor 103 inside the condensing chamber 4.
  • Fig. 10 shows the end view of an improved distillation apparatus incorporating pairs of heat transfer tubes
  • Fig. 11 shows the corresponding elevation view.
  • This device has one main drive shaft 406 which carries two pairs of eccentric bearings 405' and 405, oriented 180° phase angle apart.
  • Eccentric drives 405 and wobbling plates 401 and 401' carry groups of heat transfer tubes 403 and 404. Tubes 403 and 404 are symmetrical with respect to the center of the eccentric so that thier combined C.G coincides with the center of the eccentric 405.
  • Eccentric 405' drives wobbling plates 402 and 402' which carry tubes 403' and 404' whose combined C.G coincides with the center of the eccentric 405'.
  • the center drive shaft 406 is supported by bearings 430 and 431 which are secured to the main tank via structure members 432 and 433.
  • the upper ends of the four groups of tubes 403, 404, 403' and 404' are cappedwith channel shaped ring 412 as shown in Fig. 11 to receive fluid which is distributed via tubes 411.
  • Fig. 12 and Fig. 13 show further, details of ring 412 and tube 411.
  • a flexible membrane 410 is used to allow the tubes to pass through the perforations in the membrane.
  • a second flexible membrane 410' is used near the lower ends of the groups of tubes.
  • the tubes are arranged symmetrically with respect to the center of the membrane and driven by the eccentric 405 which is also at the geometric center of the tube groups, it follows that the resultant elastic force exerted by the membranes to the tubes always points toward the center of the eccentric.
  • the wobbling drive does not produce a moment to cause angular displacement of the tube assembly, which wobbles but remains oriented in a fixed direction.
  • the convolutions 450 of the membrane are shaped in such manner to make it flexible for wobbling motion while being quite rigid so as to resist rotational motion.
  • the principle of the selective rigidity of the membranes can be illustrated by the universal joint 408 of Fig. 20.
  • This double universal joint 408 is anchored to the frame work at the upper end 409 and is attached to the wobbling member 401 which is driven by eccentric 405 and shaft pivot 406.
  • This universal joint is very rigid in its torsional mode but is flexible in lateral mode. For this reason it provides an excellent guide for wobbling motion.
  • a membrane is not as rigid a guide as the universal joint but is adequate for most purposes and is economical because it also serves another function, i.e. as the partition for the chambers.
  • Fig. 12 and Fig. 13 illustrate the construction of a new fluid distribution scheme.
  • Fluid to be evaporated is introduced to the upper ends of the evaporating tubes 403 and 404 via distributing tubes 411 and circular channel rings 412.
  • Each tube 411 is pivoted by a pin 413 and is tensioned by a spring 417 to cause the quide pin 414 to bear against the inside edge 423 of the circular ring 412.
  • Guide pin 414 is an integral part of tube 411.
  • a line drawn between pivot 413 and guide pin 414 is approximately tangent to the circle of the inside edge 423.
  • the wobbling motion of the channel 412 will keep the liquid revolving to form a crescent shaped fluid body 418, and overflow down the tube 403 with a revolving stream 419. Since in this arrangement the nozzle 416 does not revolve, it supplies fluid at a stationary point.
  • the large surface 418' of the crescent shaped fluid body 418 serves the function of a reservoir to maintain an ample supply of flow to the downward stream 419.
  • the size of the circular channel is a design choice, a large channel will provide an even head supply of stream 419. However, stream 419 can also adjust itself after flowing down for a certain distance. Thus even without the circular ring the flow stream 419 may reach a steady state a certain distance downward.
  • Typical design parameters for water as the fluid are 2" diameter copper heat transfer tube with a wobbling radius in excess of 1/4", a revolving speed in excess of 150 R.P.M. and a flow rate in excess of 1 lb/min. Below these values the fluid flow may not be "synchronized" with the wobbling drive to form a revolving stream to wipe the inside surface of the tube.
  • Figs. 14 and 15 show an improved scheme using the wobbling drive to handle fluid with higher viscosity. This is accomplished with a heavy bar 429 which is hung under a revolving arm 427 pivoted at shaft 426 and engaged to the inside surface of the tubes 403 via roller 428. This heavy bar 429 pushes fluid 420 in front of it as it revolves on the direction of arrow 421 to generate a thin film to facilitate the evaporation.
  • Figs. 16 and 17 show another fluid distribution system.
  • two wobbling tubes 403 are shown. They are coupled together at the top by a "valve plate” 460. Short cylindrical “valves” 461 are used to engage with the valve plate 460. These cylindrical valves are held together by plate 462.
  • Incoming fluid is introduced into the space between plates 462, 460 and cylinders 461. Tubes 403 and plate 460 wobble with respect to the cylinder 461 and plate 462. For instance the center 466 of tube 403 traverses around the circular locus 467 with its center 465 coinciding with the center of cylinder 461.
  • This wobbling motion creates a crescent shaped gap 464 which revolves around tube 403 and cylinder 461.
  • This revolving gap allows fluid to drain through to form the revolving stream 469. A portion of this stream is evaporated to form vapor 468 which escapes through the inside of tube 403 and cylinder 461.
  • Fig. 18 illustrates in detail one configuration of the convolution 450 of membrane 410.
  • Fig. 19 illustrates a conceptual model of the convolution serving as a wobbling seal.
  • the membrane 410 is divided into three elements, 410a, 410b and 450 or 450'.
  • Fig. 19 shows that 410a is driven to wobble with respect to 410b in that a typical point 420 on 410a will be driven to describe a circle 421 with respect to element 410b.
  • Convolution 450' of Fig. 19 must therefore provide a seal across the membrane 410 while offering low and uniform elastic constraint against the wobbling motion and a reasonable service life.
  • a typical value of wobbling motion is about 1/2".
  • the grid 450' of Fig. 19 is a natural yieldable structure which would bridge 410a and 410b to allow wobbling motion between them.
  • One configuration is to use reinforcement fiber to form the rectangular grid pattern and then fill the area of the grid with soft rubber film which can be stretched into diamond shape as the grid is subjected to the shear mode of deformation.
  • Another configuration shown in Fig. 18, uses homogeneous material with- the sheet preformed into ridges with circular bumps 451 to facilitate shear mode deformation. Square bumps between rectangular ridges could be used.
  • membrane 410 replaces the several inner containers 2s and 2's, the associated flexible couplings 8, 9, 10 etc., and the guiding cranks 51's of the earlier figures.

Landscapes

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

Abstract

Dispositif de distillation dans lequel un groupe de paires de tubes (7) de transfert de chaleur sont entraines de maniere a osciller autour d'un axe vertical passant au travers d'un centre d'oscillation (30), (64-67). Un courant de fluide (101) s'ecoule a l'interieur de chaque tube. Le courant de fluide tend a adherer a la surface interieure du tube loin du centre d'oscillation pendant qu'il tourne par rapport au tube en reponse au mouvement d'oscillation. Le courant d'ecoulement tournant (6) essuie la surface interieure du tube (7) pour former une pellicule mince (5) qui offre une faible resistance thermique pour faciliter l'evaporation, emporte le residu par son mouvement lateral et emporte le reflux vers le bas avec une restriction moindre. Afin de garantir un equilibre dynamique accru des tubes pendant l'oscillation, dans un mode preferentiel de realisation les tubes sont montes en deux paires de groupes de tubes (403), (404) et (403'), (404'), chaque paire de groupes de tubes etant montee symetriquement autour d'un axe vertical associe. Le montage des tubes possede des dispositifs (410), (410') permettant d'empecher la rotation des tubes autour de cet axe vertical tout en permettant l'oscillation. Chaque paire de groupes de tube possede un arbre d'entrainement (406) et un systeme d'entrainement excentrique (405), (405'), (401) (401'), (402) (402') connectant l'arbre aux groupes de tubes.
EP19810902919 1980-10-27 1981-10-19 Dispositif de distillation ameliore. Withdrawn EP0063141A4 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US20138080A 1980-10-27 1980-10-27
US201380 1980-10-27

Publications (2)

Publication Number Publication Date
EP0063141A1 true EP0063141A1 (fr) 1982-10-27
EP0063141A4 EP0063141A4 (fr) 1985-03-06

Family

ID=22745602

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19810902919 Withdrawn EP0063141A4 (fr) 1980-10-27 1981-10-19 Dispositif de distillation ameliore.

Country Status (4)

Country Link
EP (1) EP0063141A4 (fr)
JP (1) JPS57501825A (fr)
GB (1) GB2098496B (fr)
WO (1) WO1982001475A1 (fr)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4618399A (en) * 1978-11-16 1986-10-21 Li Yao T Wobble tube evaporator with whip rod fluid distributor
JPH0326882Y2 (fr) * 1986-12-12 1991-06-11
CN108654174B (zh) * 2018-06-01 2020-07-03 安徽江锐新材料有限公司 一种用于水性涂料的板式过滤机

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2884050A (en) * 1954-03-23 1959-04-28 Lloyd E Brownell Centrifugal evaporator
US2894879A (en) * 1956-02-24 1959-07-14 Kenneth C D Hickman Multiple effect distillation
US3190817A (en) * 1957-08-12 1965-06-22 Gen Electric Compression distillation apparatus
US4230529A (en) * 1978-11-16 1980-10-28 Li Yao T Distillation apparatus

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
No relevant documents have been disclosed. *
See also references of WO8201475A1 *

Also Published As

Publication number Publication date
WO1982001475A1 (fr) 1982-05-13
JPS57501825A (fr) 1982-10-14
EP0063141A4 (fr) 1985-03-06
GB2098496A (en) 1982-11-24
GB2098496B (en) 1984-10-24

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