Classifications

• • D—TEXTILES; PAPER
  • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
  • D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
  • D06F43/00—Dry-cleaning apparatus or methods using volatile solvents
  • D06F43/08—Associated apparatus for handling and recovering the solvents
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D1/00—Evaporating
  • B01D1/0011—Heating features
  • B01D1/0041—Use of fluids
  • B01D1/0047—Use of fluids in a closed circuit
• • 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
  • B01D3/10—Vacuum distillation
• • 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
  • B01D5/0003—Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
  • B01D5/0006—Coils or serpentines
• • 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
  • B01D5/0045—Vacuum 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
  • B01D5/0057—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
• • 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
  • B01D5/0078—Condensation of vapours; Recovering volatile solvents by condensation characterised by auxiliary systems or arrangements
  • B01D5/009—Collecting, removing and/or treatment of the condensate
• • D—TEXTILES; PAPER
  • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
  • D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
  • D06F43/00—Dry-cleaning apparatus or methods using volatile solvents
• • D—TEXTILES; PAPER
  • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
  • D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
  • D06F43/00—Dry-cleaning apparatus or methods using volatile solvents
  • D06F43/08—Associated apparatus for handling and recovering the solvents
  • D06F43/081—Reclaiming or recovering the solvent from a mixture of solvent and contaminants, e.g. by distilling

Definitions

• the present invention relates to a distillation apparatus used for purifying a solvent used for cleaning, for example, a solvent used in a dry cleaner or various electronic parts.
• a vacuum distillation apparatus for purifying the solvent is used in order to repeatedly use a solvent (silicone oil, petroleum solvent, etc.) soiled by washing laundry. ing.
• a solvent silicone oil, petroleum solvent, etc.
• the most common method for condensing solvent vapor in such distillation equipment is to install a pipe with a large surface area such as a spiral shape inside a container filled with solvent vapor, and use a chiller or cooling tower inside the pipe. This is a method of flowing and condensing cooled water (see, for example, Patent Document 1).
• a spiral pipe is placed in a container filled with cold water, and heat is exchanged through solvent vapor into the pipe for condensation. All of these use water as a medium for heat exchange with solvent vapor.
• a buffer tank for storing the solvent is provided, and the solvent in the tank is sucked and pressurized by a pump and circulated through the ejector, thereby evacuating the distillation tank. Is going.
• the solvent since the solvent generates heat by circulating the pump, it is necessary to cool the solvent in the buffer tank by installing a pipe for flowing cooling water in the buffer tank. For this reason, a buffer tank and a cooling container for solvent vapor condensation are required separately. There is a problem that it is difficult.
• Patent Document 1 Japanese Patent Application Laid-Open No. 7_2 8 9 7 8 8
• Patent Document 2 Japanese Patent Laid-Open No. 2 0 0 6 _ 1 4 1 5 4 6
• the present invention has been made in view of the above-mentioned problems.
• the first object of the present invention is to perform efficient distillation work by sufficiently cooling the solvent vapor without using cooling water. It is to provide a distillation apparatus that can be used.
• a second object of the present invention is to provide a distillation apparatus capable of performing efficient distillation work by sufficiently condensing and liquefying solvent vapor while reducing the size of the apparatus. It is in.
• a first invention made to achieve the first object is a distillation apparatus for distilling a liquid to be treated such as a solvent, for example.
• the liquid to be processed is directly passed through a wall that separates the liquid vapor to be processed and a refrigerant gas that is a cooling source.
• the distillation apparatus instead of the conventional cooling water as a cooling source for condensing the liquid to be treated, refrigerant gas that has been cooled to a low temperature by a so-called outdoor unit including a compressor or the like is used. To do. Then, in the heat exchanging portion, the vapor of the liquid to be treated is directly cooled by the refrigerant gas through the wall surface, thereby promoting the condensation and liquefaction of the vapor. Therefore, unlike conventional distillation devices of this type, no cooling water is used, so there are problems and problems associated with the use of cooling water, that is, problems such as generation of drought and scales due to long-term use, freezing in cold regions, etc. Can be avoided.
• refrigerant gas has a temperature of about 0 ° C or less (usually about 120 to 0 ° C) and can be considerably lower than that of cooling water.
• the solvent used in this process has a large temperature difference from 90 to 110 ° C), and it is possible to efficiently cool the liquid to be treated and promote condensate liquefaction.
• a buffer tank for storing the distilled liquid to be treated
• An inlet end and an outlet end are connected to the buffer tank, and a distilled liquid to be treated which has been liquefied in the heat exchange section using a pump for circulating the liquid to be treated in the middle of the buffer tank and a flow of the liquid to be treated by the pump.
• a to-be-treated liquid circulation channel provided with an ejector for suction;
• the heat exchanging unit is disposed in the buffer tank, and separates the wall surface that separates the refrigerant gas that is a cooling source from the liquid to be processed, and the refrigerant gas and the liquid to be processed in the buffer tank. It is preferable that each has a wall surface.
• the liquid vapor to be treated vaporized from the distillation kettle is cooled by heat exchange with the refrigerant gas in the heat exchange section to be condensed and liquefied.
• the distilled liquid to be treated is drawn into the liquid circulation path by the ejector and returned to the buffer tank.
• the temperature of the liquid to be processed that has not sufficiently decreased during condensing and the liquid to be processed that has not been liquefied is mixed with the liquid to be processed sucked from the buffer tank by the ejector. Liquefaction.
• the liquid to be treated When the liquid to be treated circulates through the circulation path of the liquid to be treated and returns to the buffer tank, the temperature of the liquid to be treated rises, but the buffer tank is immersed in the liquid to be treated. In the heat exchange section, the liquid to be treated is cooled by heat exchange with the refrigerant gas. Therefore, an increase in the temperature of the liquid to be processed in the buffer tank can be avoided.
• the cooling container and the buffer tank for cooling the liquid vapor to be processed can be integrated into one, so that the structure is simplified, which is advantageous for downsizing of the apparatus and maintenance is also performed. easy.
• the liquid to be processed in the buffer tank and the liquid to be processed introduced from the still are directly cooled by the solvent gas across the wall surfaces, both can easily secure a sufficient temperature difference and are high. A cooling effect can be exerted.
• the heat exchange part is provided in the buffer tank and immersed in the liquid to be treated, the cold heat of the refrigerant gas is unlikely to escape (for example, in the air), and high cooling efficiency can be achieved. Unnecessary condensation and frost can be avoided without using.
• the liquid to be processed and the liquid to be processed in the buffer tank can be cooled simultaneously by the refrigerant gas, there is no waste and high efficiency.
• the heat exchange unit is a double-pipe structure including an outer pipe through which the refrigerant gas flows and an inner pipe through which the liquid vapor to be processed flows. It can be.
• the heat exchange part is a double-pipe structure wound spirally, a large surface area for heat exchange can be secured without increasing the volume of the buffer tank, Cooling efficiency can be increased.
• a temperature detection unit may be provided on the inlet side of the inner tube of the double tube structure that is immersed in the liquid to be processed in the buffer tank.
• the temperature detected by the temperature detecting means changes abruptly at the start of generation of the liquid vapor to be processed in the initial stage of heating in the distillation kettle or at the end of generation of the liquid vapor to be processed. Based on the temperature, the start of distillation and the end of distillation can be detected reliably and accurately. As a result, it can be used, for example, for control such as on / off of the outdoor unit and capacity switching.
• a second invention made to achieve the second object described above is a distillation apparatus for distilling a liquid to be treated such as a solvent.
• a double pipe comprising an inner pipe or an outer pipe through which the liquid vapor to be treated is circulated and an outer pipe or inner pipe through which the cooling liquid is circulated.
• a heat exchange part which is a structure;
• the cooling liquid is typically cooling water.
• the distillation apparatus according to the second invention Accordingly, it is possible to save space by making the heat exchange part compact while ensuring a large area for heat exchange between the liquid vapor to be treated and the coolant. In particular, a spiral double tube structure can be made more compact.
• a buffer tank for storing the distilled liquid to be treated
• An inlet end and an outlet end are connected to the buffer tank, and a distilled liquid to be treated which has been liquefied in the heat exchange section using a pump for circulating the liquid to be treated in the middle of the buffer tank and a flow of the liquid to be treated by the pump.
• a to-be-treated liquid circulation channel provided with an ejector for suction;
• the heat exchange part may be disposed in the buffer tank, and the liquid vapor to be processed may be circulated through the inner pipe and the cooling liquid may be circulated through the outer pipe.
• the temperature difference with the liquid to be treated is relatively small.
• the steam of the liquid to be processed and the liquid to be processed in the buffer tank can be directly cooled by the cooling water across the wall surfaces. Therefore, compared to the conventional method of cooling the liquid to be processed in the buffer tank with cooling water and cooling the liquid to be processed with this liquid to be processed, the temperature for heat exchange with the liquid to be processed It is easy to ensure the difference, and the liquid vapor to be treated can be efficiently cooled to promote condensation.
• the heat exchanging part is provided in the buffer tank and immersed in the liquid to be processed, the cooling heat of the cooling water is difficult to escape (for example, in the air), and this is treated with the liquid vapor to be processed. It can be effectively used to cool the liquid and the liquid to be processed in the buffer tank. This makes it possible to process the same amount of liquid to be processed in a shorter time by increasing the distillation rate.
• the distillation apparatus according to the first and second inventions can be used for distillation of various liquids to be treated, it is particularly suitable for purifying by purifying a dirty solvent by operation of a dry cleaner. It is.
• the liquid vapor to be treated such as a solvent can be efficiently cooled, condensed and liquefied and recovered without using cooling water.
• maintenance costs can be reduced by avoiding the occurrence of scales and freezing in cold regions due to long-term use.
• the apparatus can be downsized to increase the degree of freedom of installation, and the distillation rate of the liquid to be treated can be improved by performing efficient cooling.
• FIG. 1 is a configuration diagram of a main part centering on a piping path of a dry cleaner using a distillation apparatus according to an embodiment of the present invention.
• FIG. 2 is a configuration diagram centering on the piping path of the distillation apparatus of the present embodiment.
• Fig. 1 is a configuration diagram of the main parts centering on the piping path of a dry cleaner using the distillation apparatus of the present embodiment
• Fig. 2 is a configuration diagram centering on the piping path of the distillation apparatus of the present embodiment.
• the liquid to be treated in the present invention is a petroleum-based or silicone-based solvent used for cleaning operation.
• a cylindrical drum 2 having a large number of liquid passage holes around it is rotatably supported in the outer tank 1, and the liquid level of the solvent stored in the outer tank 1 Can be detected by the liquid level sensor 3.
• a drain valve 5 connected to the bottom of the outer tank 1 is provided with a drain valve 5, which is connected to a solvent tank 7 via a button trap strainer 6. Potane Trap Strainer 6 It is a type of filter that removes relatively large solids such as clothing buttons in the agent.
• the suction pipe 8 inserted into the solvent tank 7 is connected to the suction port of the pump 10 via the check valve 9, and the discharge port of the pump 10 is connected to the solvent filter 1 2 via the three-way valve 11 Are connected to the inlet and the outlet.
• the solvent filter 12 is composed of a paper filter, an activated carbon filter, etc., and removes impurities such as fine dust and various dirt components mixed in the solvent.
• a filter drain line 13 branched from between the pump 10 and the three-way valve 1 1 is connected to the button trap strainer 6 through the filter drain valve 14.
• the outlet of the solvent filter 1 2 is branched into a bypass pipe 18 having a solvent cooling switching valve 20 inserted in the middle and a solvent cooling pipe 19 passing through the solvent cooling device 21 in the middle.
• the paths 18 and 19 are joined and connected to the outer tank 1 as a liquid supply pipe line 2 2 in which a liquid supply valve 23 is inserted.
• the return pipe 24 branched from the front of the liquid supply valve 23 is provided with a tank circulation / club 25, and the outlet end of the return pipe 24 is connected to the solvent tank 7.
• An air vent line 17 is connected between the upper part of the solvent filter 1 2 and the upper part of the button trap strainer 6, and an air vent valve 1 6 and a pressure gauge 15 are connected to the air vent line 17. And are provided. Also, the outer tub 1 is connected to one end of a soap charging pipe 28 provided with a soap charging device 29 in the middle, and the other end is connected to a soap container 27. In addition, a soap concentration sensor 26 is attached to the branch point between the liquid supply line 2 2 and the return line 2 4 in order to detect the concentration of soap in the solvent.
• a distillation introduction valve 31 is provided in the distillation introduction pipe 30 branched from the inlet of the solvent filter 12, and the distillation introduction pipe 30 is a distillation apparatus 4 0. It is connected to the. Further, the distillation suction pipe 32 having one end inserted so as to be immersed in the solvent in the solvent tank 7 is connected to the distillation apparatus 40 via the suction switching valve 33. In addition, the distilled solvent taken out from the distillation apparatus 40 is introduced into the water separator 71, and the solvent from which the water has been removed is supplied to the solvent tank 7. Returned.
• the following liquid supply flow path is formed when washing the laundry stored in the drum 2. That is, first, in order to supply the solvent stored in the solvent tank 7 into the outer tank 1, the drain valve 5 and the tank circulation valve 2 5 are closed, the liquid supply valve 2 3 is opened, and the pump 10 is operated. Let The solvent cooling switching valve 20 is turned off appropriately according to the temperature of the solvent detected by a temperature sensor (not shown), so that a part of the solvent flows through the solvent cooling pipe 19 to cool the solvent.
• the solvent stored in the solvent tank 7 is sucked up by the pump 10 through the suction pipe 8, and the solvent filter 1 2, the bypass pipe 1 8 or the solvent cooling pipe 1 9, and the liquid supply pipe 2 It is supplied into the outer tank 1 through 2. Dirt and fine foreign matter mixed in the solvent when passing through the solvent filter 1 2 are removed.
• the liquid level sensor 3 detects that a predetermined amount of solvent has accumulated in the outer tank 1, the solvent is supplied from the solvent tank 7 into the outer tank 1, and the predetermined liquid level is stored in the outer tank 1.
• the laundry is washed by rotating the drum 2 while the solvent is stored.
• the drain valve 5 is closed and cleaning is performed with the same solvent stored in the outer tank 1, and the drain valve 5 is opened and the supply of the solvent through the liquid supply channel is continued. It is also possible to perform cleaning.
• the soap is introduced by the soap dispenser 29 so as to improve the washing performance and prevent the electrification so as to obtain an appropriate soap concentration.
• relatively large foreign matter such as lint and lint from the laundry is removed when the drain valve 5 is opened and the solvent in the outer tub 1 returns to the solvent tank 7 through the drain line 4. Collected with the button trap strainer 6.
• the following solvent circulation channel is formed. That is, the liquid supply valve 23 is closed, the tank circulation valve 25 is opened, and the pump 10 is operated.
• the solvent cooling switching valve 20 is turned off according to the temperature of the solvent detected by a temperature sensor (not shown) so that a part of the solvent flows to the solvent cooling pipe 19 to cool the solvent. .
• the solvent stored in the solvent tank 7 is sucked up by the pump 10 through the suction line 8 and is passed through the solvent filter 1 2, the bypass line 1 8 or the solvent cooling line 1 9, and the return line 2 4. After that, it returns to the solvent tank 7.
• dirt and fine foreign matters mixed in the solvent are removed, and the solvent temperature is appropriately controlled by cooling with the solvent cooling device 21.
• the solvent filter 12 can remove most of the dirt in the solvent, but it cannot remove very fine dirt or water that passes through the filter eyes. Purify by distillation for repeated use in a clean state.
• the distillation introduction valve 31 is opened, and the solvent sucked by the pump 10 from the solvent tank 7 is sent to the distillation apparatus 40 through the distillation introduction line 30.
• the suction switching valve 3 3 is opened during vacuum distillation, the solvent is sucked up from the solvent tank 7 into the distillation kettle that is in a vacuum state, and accordingly, the solvent is sent to the distillation device 40. You can also. Then, it is evaporated and evaporated by the distillation device 40.
• the distillation introduction line 30 provided with the distillation introduction valve 3 1 is connected to a sealable distillation kettle 4 1, and the bottom of the distillation kettle 4 1 is heated by steam supplied through the steam supply pipe 4 3.
• a heating chamber 42 to be heated is provided.
• the solvent vapor (liquid vapor to be treated in the present invention) vaporized in the distillation pot 41 by heating passes through the demister 45 and is sent to the heat exchange section through the solvent vapor introduction pipe 46.
• a bumping detection sensor 47 for detecting bumping of the solvent is provided in the solvent vapor introduction pipe 46, and when bumping is detected, for example, by adjusting the opening of the steam adjustment valve 44, etc. Heating is weakened.
• the heat exchanging unit includes two cylindrical pipes having a cylindrical outer pipe 53 and a cylindrical outer pipe 52 formed in a spiral shape.
• Heavy pipe structure The double-pipe structure 51 is provided inside a buffer tank 50 in which a solvent is stored. In a steady state, the double-pipe structure 51 is completely immersed in the solvent stored in the buffer tank 50.
• the solvent vapor introduction pipe 4 6 is connected to the upper end of the inner pipe 5 2 of the double pipe structure 5 1 outside the buffer tank 50, and the inner pipe 5 2 has a high temperature (90 to 1 1 0 Solvent vapor at about ° C) is introduced.
• both ends of the outer pipe 53 of the double pipe structure 51 are connected to the refrigerant gas supply pipe 5 6 and the refrigerant gas recovery pipe 5 7 inside the buffer tank 50, respectively.
• the refrigerant gas supply pipe 5 6 and the refrigerant gas recovery pipe 5 7 inside the buffer tank 50 respectively.
• an outdoor unit installed outdoors. 5
• Low-temperature solvent gas (approx. 120 to 0 ° C) supplied through the refrigerant gas supply pipe 5 6 circulates in the outer pipe 5 3 and passes through the refrigerant gas recovery pipe 5 7 to the outdoor. Return to machine 5-5.
• the solvent condensed and liquefied when passing through the inner pipe 52 of the double-pipe structure 51 is passed through a regenerated solvent recovery pipe 58 provided with a backflow prevention valve 63.
• a regenerated solvent recovery pipe 58 provided with a backflow prevention valve 63.
• the thermistor that detects the temperature in the inner pipe 5 2 so that it protrudes from the connection between the solvent vapor inlet pipe 4 6 and the inner pipe 5 2 of the double pipe structure 5 1 to the inside of the buffer tank 50. Is installed.
• an air suction valve 60, a vacuum meter 6 1, and a vacuum pressure switch 6 2 for taking in the atmosphere are connected to the upstream side of the backflow prevention valve 63 on the recycled solvent recovery pipe 58.
• the ejector 66 is inserted together with the pump 65 in the middle of the regenerative solvent circulation pipe 64 having the outlet end and the inlet end connected to the buffer tank 50.
• the pump 65 When the pump 65 is activated, the solvent is circulated and pumped in the direction indicated by the arrow in FIG. 2 to the regenerated solvent circulation line 6 4, and the regenerated solvent recovery line 5 8 is generated by the negative pressure generated in the ejector 6 6.
• Distilled solvent is drawn into recycled solvent circulation line 6 4.
• the solvent vapor in the solvent vapor introducing pipe 46 is drawn into the inner pipe 52 of the double pipe structure 51, and the inside of the distillation pot 41 is evacuated and depressurized. Due to the pressure reducing action at this time, as described above, the solvent in the solvent tank 7 can be sucked into the distillation still 41 through the distillation suction line 32.
• the temperature of the regenerated solvent that has just been condensed and liquefied through the regenerated solvent recovery line 58 is Although relatively high, the temperature is lowered by mixing with the solvent in the recycle solvent circulation pipe 6 4 through the ejector 6 6.
• the temperature of the solvent in the recycled solvent circulation pipe 64 rises to the buffer tank 50 due to the amount of heat given from the recycled solvent and the amount of heat given from the pump 65 and the like as described above.
• the solvent in the buffer tank 50 is cooled by the refrigerant gas flowing in the outer pipe 53 of the double pipe structure 51, the temperature of the solvent is stably maintained as a whole. .
• the solvent level in the buffer tank 50 is increased by the addition of the regenerated solvent generated by distillation.
• Solvent overflow pipe 70 The solvent that has passed the upper end opening of the buffer flows out of the buffer tank 50 and separates the water. The water is separated and returned to the solvent tank 7. Therefore, the solvent tank 7 can be returned with a relatively stable solvent.
• a high-temperature solvent vapor flows through the inner pipe 52, and a low-temperature refrigerant gas surrounds the wall through the wall separating the inner pipe 52 and the outer pipe 53. Is in circulation. Since the temperature difference is large, the two perform heat exchange efficiently, and the solvent gas is efficiently cooled to condensate.
• the entire circumference of the outer tube 5 3 of the double-pipe structure 51 is surrounded by a solvent through a wall surface. Therefore, the refrigerant gas in the outer pipe 5 3 exchanges heat efficiently with this solvent, and the solvent in the buffer tank 50 is efficiently cooled and the temperature is lowered.
• the refrigerant gas passing through the outer pipe 53 is always in thermal contact with either the solvent or the solvent vapor through the wall surface. Therefore, if solvent vapor has not yet been supplied or if the amount of solvent vapor supplied is small, the refrigerant gas's cold heat is used more by cooling the solvent in the buffer tank 50 and is wasted. None become.
• the solvent in the buffer tank 50 functions as a thermal buffer having a kind of heat capacity, the amount of cold heat taken from the refrigerant gas passing through the outer pipe 53 is kept almost constant, and the outdoor unit 5 Return to 5 to suppress large fluctuations in refrigerant gas temperature. This makes it easy to achieve thermal matching in the outdoor unit 55 and prevents frost from being generated due to excess cooling in the outdoor unit 55.
• the solvent in the buffer tank 50 also functions as a kind of heat insulating material, the refrigerant gas supply pipe 5 6 With the exception of some parts, it is not necessary to take measures against condensation and frost, such as wrapping a heat insulating material.
• the temperature detection portion by the thermistor 54 is at the inlet of the solvent vapor cooling section, for example, when the solvent vapor has not yet been generated in the distillation pot 41, the detection temperature is low, and the high temperature solvent vapor is When it reaches, the temperature rises rapidly. On the other hand, when solvent vapor is no longer generated or the amount decreases sharply in the distillation kettle 41, the detection temperature also drops rapidly. Therefore, it follows the start and end of distillation (solvent vapor generation) almost without delay, and wasteful power consumption is reduced by adjusting the cooling capacity of the outdoor unit 55 based on this detected temperature. The running cost of distillation can be reduced.
• the refrigerant gas is allowed to flow through the outer pipe 53 of the double-pipe structure 51.
• both the solvent vapor and the solvent in the buffer tank 50 are cooled by flowing cooling water.
• the cooling water is higher than the temperature of the refrigerant gas, the cooling effect is inferior to that of the refrigerant gas, but a sufficient temperature difference can be secured as compared with the conventional apparatus.
• the use of such cooling water is convenient when it is desired to use equipment and piping that can supply cooling water such as a cooling tower and a chiller as they are.
• the above-described embodiment is an example of the present invention, and it is apparent that any modification, correction, or addition as appropriate within the scope of the present invention is included in the scope of the claims of the present application.
• the above embodiment is an example in which the present invention is applied to a dry cleaner, but besides that, for example, various solvents used for cleaning various electrical components such as semiconductors can be recovered and reused. It can be used in various devices and fields, and the liquid to be treated for distillation (treatment) is not limited to solvents, but can be various kinds of liquids such as alcohols.

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• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Engineering & Computer Science (AREA)
• Textile Engineering (AREA)
• Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
• Accessory Of Washing/Drying Machine, Commercial Washing/Drying Machine, Other Washing/Drying Machine (AREA)

Priority Applications (2)

Applications Claiming Priority (2)

Publications (1)

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Citations (7)

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• 2006
  • 2006-08-31 JP JP2006235860A patent/JP2008055334A/ja not_active Ceased
• 2007
  • 2007-03-12 WO PCT/JP2007/000199 patent/WO2008026301A1/ja not_active Ceased
  • 2007-03-12 US US12/308,682 patent/US8241466B2/en not_active Expired - Fee Related
  • 2007-03-12 EP EP07713581A patent/EP2058038A1/en not_active Withdrawn
  • 2007-04-12 KR KR1020070036132A patent/KR100827586B1/ko not_active Expired - Fee Related
  • 2007-08-22 CN CNA2007101430702A patent/CN101156994A/zh active Pending

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