CN103182194A - Integrated-type liquid vaporization-separation tank device - Google Patents
Integrated-type liquid vaporization-separation tank device Download PDFInfo
- Publication number
- CN103182194A CN103182194A CN2011104431582A CN201110443158A CN103182194A CN 103182194 A CN103182194 A CN 103182194A CN 2011104431582 A CN2011104431582 A CN 2011104431582A CN 201110443158 A CN201110443158 A CN 201110443158A CN 103182194 A CN103182194 A CN 103182194A
- Authority
- CN
- China
- Prior art keywords
- steam
- liquid
- tank body
- pipe
- vaporization
- 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
Links
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention relates to a liquid vaporization-separation device, and particularly relates to an integrated-type liquid vaporization-separation tank device. The integrated-type liquid vaporization-separation tank device is formed by connecting a vaporization-condensation tank device with a heat exchange tank device up and down, and is characterized in that the tank body of the vaporization-condensation tank device and the tank body of the heat exchange tank device are the upper section and the lower section of the tank body of the vertical integrated-type liquid vaporization-separation tank device; a liquid ascending channel and a liquid descending channel are arranged in the tank body of the integrated-type liquid vaporization-separation tank device; the to-be-vaporized-separated liquid input port of the vaporization-condensation tank device is communicated with the cold fluid output port of the heat exchange tank device via the liquid ascending channel; and the vaporized-separated liquid output port of the vaporization-condensation tank device is communicated with the hot fluid input port of the heat exchange tank device via the liquid descending channel. Because the liquid vaporization-separation working procedures of heating a cold fluid, vaporizing a hot fluid, liquefying vapour, cooling the hot fluid, and the like are finished in one tank device, the integrated-type liquid vaporization-separation tank device disclosed by the invention has the advantages of being low in energy consumption, low in investment, and low in operation cost, and the like.
Description
The present invention relates to a kind of vaporizing liquid separator, is a kind of integral type vaporizing liquid knockout drum device.
Industries such as vaporizing liquid separation equipment device is produced at petrochemical industry production, liquid concentration, distilled water, desalinization, liquid waste processing are used widely.Master operations such as the vaporizing liquid separating technology need heat up through supercooled liquid usually, hydrothermal solution vaporization, steam condensation, hydrothermal solution cooling, and master operations such as existing cold liquid intensification, hydrothermal solution vaporization, steam condensation, hydrothermal solution cooling are generally finished by vaporization and condensation device and heat-exchanger rig two cover independent device, in the vaporization and condensation device, finish operations such as hydrothermal solution vaporization, gas condensation, in heat-exchanger rig, finish operations such as cold liquid intensification, hydrothermal solution cooling.Because existing vaporization and condensation device and heat-exchanger rig are split type settings, must be connected by being exposed to the outer heat pipe of two devices vaporize separating liquid input pipe and the separating liquid efferent duct of vaporizing waited of hot fluid input pipe, vaporization and condensation device (the cold fluid efferent duct of heat-exchanger rig with) between two devices, heat pipe is many, and area of dissipation is big.Therefore existing split type vaporizing liquid separation equipment device exists defectives such as floor space is many, thermal loss big, investment is big, operating cost height.
Purpose of the present invention just provides a kind of deficiency that can overcome existing vaporizing liquid separation equipment, and the master operation process that vaporizations such as cold liquid intensification, hydrothermal solution vaporization, gas liquefaction, hydrothermal solution cooling are separated is placed on the integral type vaporizing liquid knockout drum device of finishing in the tank body device.
The technical solution adopted in the present invention is: vaporization and condensation tank arrangement and heat exchange tank arrangement are joined up and down is combined into an integral type vaporization knockout drum device, the vaporization and condensation tank arrangement is last, change tank arrangement following, the tank body of the tank body of vaporization and condensation tank arrangement and heat exchange tank arrangement be respectively a upright tank body on, following two sections, in the tank body of integral type vaporization knockout drum device, be provided with the liquid data feedback channel, the liquid down going channel, the waiting of the vaporization and condensation tank arrangement separating liquid input port of vaporizing communicates by the liquid data feedback channel with the cold fluid delivery outlet of heat exchange tank arrangement, the separating liquid delivery outlet of vaporizing of vaporization and condensation tank arrangement communicates by the liquid down going channel with the hot fluid input port of heat exchange tank arrangement, bottom at the tank body of heat exchange tank arrangement has stoste cold fluid entrance, the hot fluid outlet of having vaporized and having separated cooling has the deslagging drain in the bottom of the tank body of integral type vaporization knockout drum device.
During the device operation, under the effect of hydraulic pressure, the waiting of cold conditions vaporized and separated stoste and enter the heat exchange tank arrangement from the stoste cold fluid entrance of the tank body bottom of heat exchange tank arrangement, in the tank body of heat exchange tank arrangement, flow from bottom to top, temperature progressively raises after carrying out heat exchange with the hot separating liquid of vaporization that flows in the tank body of heat exchange tank arrangement from top to bottom, becomes hot separating liquid to be vaporized; The hot separating liquid of waiting to vaporize enters in the epimere (tank body of vaporization and condensation tank arrangement) of upright tank body by liquid data feedback channel in the upright tank body, in the vaporization and condensation tank arrangement, further heated, vaporized, separation, condensation, become the hot separating liquid of vaporization; The hot separating liquid of vaporizing enters in the hypomere (tank body of heat exchange tank arrangement) of upright tank body in the vaporization and condensation tank arrangement by liquid down going channel in the upright tank body, under the effect of gravity, in the tank body of heat exchange tank arrangement, flow from top to bottom, carry out being cooled gradually after the heat exchange with the separating liquid to be vaporized of the cold conditions that flows from bottom to top in the tank body of heat exchange tank arrangement, after temperature is reduced to the regulation requirement, separate outside the hot fluid outlet outflow jar that cools off from the vaporizing of tank body bottom of heat exchange tank arrangement again.Thereby in a tank body device, operations such as cold liquid intensification, hydrothermal solution vaporization, gas liquefaction, hydrothermal solution cooling have been finished.Need deslagging or emptying when maintenance, opens that continuous valve gets final product on the deslagging drain of bottom of upright tank body.
Along with pot liquid by vaporization gradually separate the back drain tank outer, cause tank level to descend, control liquid level in the jar, make pot liquid maintain normal work liquid level with jar outer devices such as liquid make-up pump by the liquid-level switch sensor is installed in jar.
When in being applied to productions such as liquid waste processing, desalinization, liquid concentration, needing in the timely drain tank high concentration liquid, control pot liquid concentration by the devices such as electrically operated valve that strength of fluid probe, concentrated liquid heat exchanger tube, the concentrated liquid outlet installed in the jar are installed above, in time surpassed certain density high concentration liquid in the blowdown vessel, make pot liquid concentration maintain normal range (NR), can not only enhance productivity, can also reclaim heat entrained in the concentrated liquid.
In being applied to desalinization production, in order to solve liquid in the problem of condenser pipe surface vaporization fouling, by in the vaporization and condensation tank arrangement, increasing a flash of steam chamber and installing devices such as flash boiling spray head unit, flash distillation sea water circulating pump additional, can avoid seawater in condenser pipe surface direct boiling and fouling on the condenser pipe surface.
Since the present invention cold liquid heat up, master operation processes such as hydrothermal solution vaporization, steam condensation, hydrothermal solution cooling are placed on and finish in the tank body device, reduce thermal hardware and supporting pipelines in the existing vaporizing liquid separating technology, had advantages such as energy consumption is low, investment is low, operating cost is low.
The present invention is further described below in conjunction with the drawings and specific embodiments.
Fig. 1 is vertical section of the present invention schematic diagram.
Fig. 2 is the specific embodiment of the invention one vertical section schematic diagram.
Fig. 3 is the specific embodiment of the invention two vertical part surface schematic diagrames.
Fig. 4 is the specific embodiment of the invention three vertical section schematic diagrames.
With reference to accompanying drawing 1.Integral type vaporizing liquid knockout drum device, by vaporization and condensation tank arrangement (1), heat exchange tank arrangement (2) is connected to form up and down, vaporization and condensation tank arrangement (1) is last, heat exchange tank arrangement (2) is following, the tank body (3) of vaporization and condensation tank arrangement (1), the tank body (4) of heat exchange tank arrangement (2) be upright integral type vaporizing liquid knockout drum device tank body (5) on, hypomere, in tank body (5), be provided with liquid data feedback channel (6), liquid down going channel (7), the waiting of vaporization and condensation tank arrangement (1) the separating liquid input port of vaporizing communicates by liquid data feedback channel (6) with the cold fluid delivery outlet of heat exchange tank arrangement (2), the separating liquid of the vaporization delivery outlet of vaporization and condensation tank arrangement (1) communicates by liquid down going channel (7) with the hot fluid input port of heat exchange tank arrangement (2), have stoste cold fluid entrance (8) in the bottom of upright tank body (4), the hot fluid outlet (9) of having vaporized and having separated cooling has deslagging drain (10) in the bottom of tank body (5).
During the device operation, under the effect of hydraulic pressure, the vaporization separation stoste for the treatment of of cold conditions enters heat exchange tank arrangement (2) from stoste cold fluid entrance (8), in the tank body (4) of heat exchange tank arrangement (2), flow from bottom to top, temperature progressively raises after carrying out heat exchange with the hot separating liquid of vaporization that flows in the tank body (4) of heat exchange tank arrangement (2) from top to bottom, becomes hot separating liquid to be vaporized; The hot separating liquid of waiting to vaporize enters in the tank body (3) of vaporization and condensation tank arrangement (1) by liquid data feedback channel (6), is further heated in vaporization and condensation tank arrangement (1), vaporizes, separation, condensation, becomes the hot separating liquid of vaporization; The hot separating liquid of vaporization enters in the tank body (4) of heat exchange tank arrangement (2) by liquid down going channel (7), under the effect of gravity, in tank body (4) from down and current downflow, carry out being cooled gradually after the heat exchange with the separating liquid to be vaporized of mobile cold conditions from bottom to top in the tank body (4), after temperature is reduced to the regulation requirement, the hot fluid outlet (9) that separates cooling of having vaporized from the bottom of tank body (4) is again flowed out outside the jar, thereby in a tank body device, operations such as cold liquid intensification, hydrothermal solution vaporization, gas liquefaction, hydrothermal solution cooling have been finished.When needing deslagging or emptying maintenance, unlatching deslagging drain (10) is gone up the valve that connects and is got final product.
Invention specific embodiment one:
With reference to accompanying drawing 2.This specific embodiment is mainly used in the production of producing of distilled water.The vaporization and condensation tank arrangement (1) of this specific embodiment is made up of the steam pressing tube (17) of tank body (3), steam condenser pipe (11), auxiliary heater (12), liquid-level switch sensor (13), blocking solution device (14), the steam absorbing tube (16) of pressing steam turbine (15), pressure steam turbine, pressure steam turbine, and heat exchange tank arrangement (2) is made up of tank body (4), heat exchanger tube (18); Have steam outlet (19) at the top of tank body (3), have vapor inlet port (20) at the sidewall of tank body (3); Tank body (3) is divided into liquid data feedback channel (6) with the jar center section part of tank body (4) joint; The separating liquid of the vaporization output mouth of pipe of steam condenser pipe (11) and heat exchanger tube (18) the upper end hot fluid input mouth of pipe join, and the pipe section of the hot fluid input mouth of pipe joint, upper end of the separating liquid of the vaporization output mouth of pipe of steam condenser pipe (11) and heat exchanger tube (18) is liquid down going channel (7); Steam condenser pipe (11), auxiliary heater (12), liquid-level switch sensor (13), blocking solution device (14) are installed in the tank body (3), heat exchanger tube (18) is installed in the tank body (4), presses steam turbine (15), steam absorbing tube (16), steam pressing tube (17) to be installed on the tank body (3); Steam absorbing tube (16) is connected with steam outlet (19), steam pressing tube (17) is connected with vapor inlet port (20), vapor inlet port (20) is connected with the steam inlet of steam condenser pipe (11), and heat exchanger tube (18) lower end cooling liquid outlet separates the hot fluid outlet (9) of cooling off and joins with vaporizing of tank body (4) bottom.
During the device operation, the separating liquid to be vaporized of cold conditions (former water) enters tank body (4) from stoste cold fluid entrance (8), in tank body (4), flowing from bottom to top under the effect of hydraulic pressure, progressively become hot separating liquid to be vaporized behind the top-down hot separating liquid of vaporization (distilled water) heat temperature raising in the heat exchanger tube (18), enter in the tank body (3) by liquid data feedback channel (6) again, in tank body (3) by steam condenser pipe (11), auxiliary heater 12), press under the acting in conjunction of steam turbine (15) and be vaporizated into water vapour; Water vapour rises and enters steam absorbing tube (16) after process blocking solution device (14) is removed fog-like liquid, becomes superheated vapour again after pressing steam turbine (15) pressurization; Superheated vapour enters by steam pressing tube (17) and discharges latent heat and sensible heat in the steam condenser pipe (11), and near treating outer steam condenser pipe (11) vaporized after separating liquid heating, the vaporization, self is condensed into the hot separating liquid of vaporization (distilled water); The hot separating liquid of vaporization (distilled water) and incondensable gas enter in the heat exchanger tube (18) from steam condenser pipe (11) by liquid down going channel (7), in heat exchanger tube (18), flow from top to bottom, the separating liquid to be vaporized of the cold conditions that flows from bottom to top that exchange heat pipe (18) is outer, tank body (4) is interior is progressively heated, self is cooled gradually, and temperature is reduced to regulation and requires the back outside jar is flowed out in hot fluid outlet (9).
Separating liquid to be vaporized in the tank body (5) (former water) causes liquid level decline in its jar because constantly being vaporized, be down to when liquid level under the liquid level of setting in limited time, automatically opening the outer liquid make-up pump of tank body (5) by liquid-level switch sensor (13) replenishes in the tank body (5) and waits the liquid (former water) of vaporizing and separating to make interior the liquid level rising of tank body (5); Prescribe a time limit when liquid level in the tank body (5) reaches on the liquid level of setting, close the outer liquid make-up pump of tank body (5) automatically by liquid-level switch sensor (13), the interior liquid level of tank body (5) is maintained between the liquid level upper limit and liquid level lower limit that sets all the time.
Invention specific embodiment two:
With reference to accompanying drawing 3.This specific embodiment is mainly used in the fluid separation applications of the industrial wastes that needs timely discharging high concentration liquid, desalinization, liquid concentration and handles.The vaporization and condensation tank arrangement (1) of this specific embodiment is made up of tank body (3), steam condenser pipe (11), auxiliary heater (12), liquid-level switch sensor (13), blocking solution device (14), the steam absorbing tube (16) of pressing steam turbine (15), pressure steam turbine, the steam pressing tube (17) of pressure steam turbine, strength of fluid probe (21), and heat exchange tank arrangement (2) is made up of tank body (4), heat exchanger tube (18), concentrated liquid heat exchanger tube (22); Being provided with a spacer assembly (23) in tank body (5) separates the interior sky of the interior sky of tank body (3) and tank body (4), liquid data feedback channel (6) is overflow lip on the liquid that spacer assembly (23) leaves, the separating liquid of the vaporization output mouth of pipe of steam condenser pipe (11) and heat exchanger tube (18) the upper end hot fluid input mouth of pipe join, and the pipe section of the hot fluid input mouth of pipe joint, upper end of the separating liquid of the vaporization output mouth of pipe of steam condenser pipe (11) and heat exchanger tube (18) is liquid down going channel (7); Have drain port under the concentrated liquid (24) at spacer assembly (23), have concentrated liquid outlet (25) in tank body (4) bottom; Steam condenser pipe (11), auxiliary heater (12), liquid-level switch sensor (13), blocking solution device (14), strength of fluid probe (21) are installed in the tank body (3), heat exchanger tube (18), concentrated liquid heat exchanger tube (22) are installed in the tank body (4), press steam turbine (15), steam absorbing tube (16), steam pressing tube (17) to be installed on the tank body (3); Have steam outlet (19) on the top of tank body (3), have vapor inlet port (20) at the sidewall of tank body (3); Steam absorbing tube (16) is connected with steam outlet (19), steam pressing tube (17) is connected with vapor inlet port (20), vapor inlet port (20) is connected with the steam inlet of steam condenser pipe (11), the lower end cooling fluid body heat outlet of heat exchanger tube (18) separates the hot fluid outlet (9) of cooling off and joins with vaporizing of tank body (4) bottom, drain port (24) joins under the upper end liquid-inlet of concentrated liquid heat exchanger tube (22) and the concentrated liquid, and the concentrated liquid outlet (25) of the lower end liquid outlet of concentrated liquid heat exchanger tube (22) and tank body (4) bottom joins.
The stoste of this specific embodiment two heats up, vaporizing liquid, gas liquefaction, hydrothermal solution cooling flow process and liquid level controlling method and specific embodiment one are basic identical, at this discharging flow process and the method for high concentration liquid only are described: during the device operation, when detecting treating tank body (3) in, strength of fluid probe (21) vaporizes the strength of fluid that separates when reaching the setting upper limit of concentration, open jar an outer electrically operated valve that links to each other with concentrated liquid outlet (25) gradually by automatic control system, the interior high concentration liquid of tank body (3) just relies on gravity drain port (24) under the concentrated liquid to enter in the concentrated liquid heat exchanger tube (22); High concentration liquid in concentrated liquid heat exchanger tube (22) from the top down in the process of flowing with tank body (4) in, the vaporize liquid that separates of bottom-up mobile waiting outside the concentrated liquid heat exchanger tube (22) carries out heat exchange and is cooled, discharge the liquid that sensible heat heats in the tank body (4), outer the waiting of concentrated liquid heat exchanger tube (22) vaporized and separated simultaneously, bottom, the temperature of high concentration liquid arrival tank body (4) passed through outside concentrated liquid outlet (25) drain tank after being down to set point of temperature; High concentration liquid effluxes and must cause the vaporize liquid level of separating liquid for the treatment of in the tank body (3) to descend, be down to when liquid level under the liquid level of setting in limited time, liquid-level switch sensor (13) just can be opened the outer liquid make-up pump of tank body (5) automatically and replenish in the tank body (5) and wait the liquid of vaporizing and separating, the interior liquid level of tank body (3) is risen, and the new parting liquid of vaporizing waited that replenishes is known from experience the strength of fluid that makes in the tank body (3) and is reduced; When detecting treating tank body (3) in, strength of fluid probe (21) vaporizes the strength of fluid of separation when being reduced to the minimum that sets, just close a jar outer electrically operated valve that links to each other with concentrated liquid outlet (25) by automatic control system, strength of fluid in the tank body (3) is no longer reduced, thereby the vaporize strength of fluid of separation for the treatment of in the tank body (3) is controlled all the time in certain scope.
Invention specific embodiment three:
With reference to accompanying drawing 4.This specific embodiment is mainly used in the problem that solves steam condenser pipe (11) surface scale in the productions such as desalinization.The vaporization and condensation tank arrangement (1) of this specific embodiment is by tank body (3), steam condenser pipe (11), auxiliary heater (12), liquid-level switch sensor (13), blocking solution device (14), press steam turbine (15), press the steam absorbing tube (16) of steam turbine, press the steam pressing tube (17) of steam turbine, strength of fluid probe (21), seawater flash pipe (26), flash boiling spray head unit (27), flash distillation sea water circulating pump (28), flash distillation sea water circulating pump suction hose (29), flash distillation sea water circulating pump pressure pipe (30) is formed, and heat exchange tank arrangement (2) is by tank body (4), heat exchanger tube (18), concentrated liquid heat exchanger tube (22) is formed; Being provided with a spacer assembly (23) in tank body (5) separates the interior sky of the interior sky of tank body (3) and tank body (4); Be provided with a flash distillation spacer assembly (31) in addition in tank body (3) the interior sky of tank body (3) is divided into two parts up and down, sky is flash of steam chamber (32) in the top, and sky is steam condensation chamber (33) in the lower part; Seawater flash pipe (26) is installed on the flash distillation spacer assembly (31), and seawater flash pipe (26) lower end import is connected with the top of steam condensation chamber (33), and the outlet of seawater flash pipe (26) upper end is connected with flash boiling spray head unit (27); Being provided with seawater overflow pipe in tank body (5) is liquid data feedback channel (6), liquid data feedback channel (6) (seawater overflow pipe) passes steam condensation chamber (33), and liquid data feedback channel (6) (seawater overflow pipe) is gone up the interior sky of logical flash of steam chamber (32), following logical tank body (4); The separating liquid of the vaporization output mouth of pipe of steam condenser pipe (11) and heat exchanger tube (18) the upper end hot fluid input mouth of pipe join, and the pipe section of the separating liquid of the vaporization output mouth of pipe of steam condenser pipe (11) and hot fluid input mouth of pipe joint, heat exchanger tube (18) upper end is liquid down going channel (7); In tank body (5), be provided with and let out pipe (34) under the concentrated seawater, let out pipe (34) upper end under the concentrated seawater and communicate with flash of steam chamber (32), let out under the concentrated seawater pipe (34) be passed down through steam condensation chamber (33) afterwards the upper end liquid-inlet of its lower end and concentrated liquid heat exchanger tube (22) join; Lower sidewall in flash of steam chamber (32) has flash distillation seawer outlet (35), lower sidewall at steam condensation chamber (33) has flash distillation sea intake (36), have concentrated liquid outlet (25) in tank body (4) bottom, have steam outlet (19) at the top of tank body (3), have vapor inlet port (20) at the sidewall of tank body (3); Steam condenser pipe (11) is installed in the steam condensation chamber (33), auxiliary heater (12) is installed on the seawater flash pipe (26), liquid-level switch sensor (13), blocking solution device (14), strength of fluid probe (21) are installed in the flash of steam chamber (32), heat exchanger tube (18), concentrated liquid heat exchanger tube (22) are installed in the tank body (4), press steam turbine (15), steam absorbing tube (16), steam pressing tube (17), flash distillation sea water circulating pump (28), flash distillation sea water circulating pump suction hose (29), flash distillation sea water circulating pump pressure pipe (30) to be installed on the tank body (3); Steam absorbing tube (16) is connected with steam outlet (19), steam pressing tube (17) is connected with vapor inlet port (20), vapor inlet port (20) is connected with the steam inlet of steam condenser pipe (11), the lower end cooling liquid outlet of heat exchanger tube (18) separates the hot fluid outlet (9) of cooling off and joins with vaporizing of tank body (4) bottom, the concentrated liquid outlet (25) of the lower end liquid outlet of concentrated liquid heat exchanger tube (22) and tank body (4) bottom joins; Flash distillation sea water circulating pump suction hose (29) joins with flash distillation seawer outlet (35), and flash distillation sea water circulating pump pressure pipe (30) joins with flash distillation sea intake (36).
The liquid level controlling method of this specific embodiment three and specific embodiment one are basic identical, discharging flow process and the specific embodiment two of high concentration liquid (concentrated seawater) are basic identical, seawater flash distillation circulation process and method at this explanation this specific embodiment three: during the device operation, the seawater of cold conditions enters tank body (4) from stoste cold fluid entrance (8), in tank body (4), flowing from bottom to top under the effect of hydraulic pressure, progressively by heat exchanger tube (18), top-down hot condensation fresh water in the concentrated liquid heat exchanger tube (22), hot concentrated seawater heat temperature raising, enter interior bottom, flash of steam chamber (32) by liquid data feedback channel (6) (seawater overflow pipe) again, again by flash distillation seawer outlet (35), flash distillation sea water pump suction hose (29), be flashed sea water circulating pump (28) pressurization, enter into the interior bottom of steam condensation chamber (33) by flash distillation sea water circulating pump pressure pipe (30) again, under the hydraulic action of flash distillation sea water circulating pump (28), when seawater flows to the top of steam condensation chamber (33) from the bottom of steam condensation chamber (33), further heated by sensible heat and latent heat that the superheated steam in the steam condenser pipe (11) discharges, the seawater that arrives steam condensation chamber (33) top enters seawater flash pipe (26), is heated to be high temperature seawater by the auxiliary heater (12) on the seawater flash pipe (26) again; High temperature seawater is sprayed in the flash of steam chamber (32) by flash boiling spray head unit (27), and because of moment release of pressure adiabatic evaporation, the part high temperature seawater that is sprayed in the flash of steam chamber (32) becomes steam (flash distillation) in flash of steam chamber (32); Steam rises and enters steam absorbing tube (16) after process blocking solution device (14) is removed fog-like liquid, becomes superheated steam again after pressing steam turbine (15) pressurization; Superheated steam enters in the interior steam condenser pipe (11) of steam condensation chamber (33) by steam pressing tube (17) and discharges latent heat and sensible heat, the seawater that has heated up that steam condenser pipe (11) in the steam condensation chamber (33) is outer is further heated, self be condensed into hot fresh water; Hot fresh water and incondensable gas flow after entering in the heat exchanger tube (18) by liquid down going channel (7) from top to bottom, seawater to the cold conditions that flows from bottom to top in the tank body (4) is progressively heated, self is cooled gradually, and its temperature is reduced to regulation and requires the back to vaporize outside the hot fluid outlet (9) that separates cooling flows out jar from tank body (4) bottom; Being sprayed at seawater that the part in the flash of steam chamber (32) is not vaporized is falling in the process of flash of steam chamber (32) bottom because the adiabatic evaporation temperature reduces, concentration raises, after dropping on the concentrated seawater that is not vaporized of bottom, flash of steam chamber (32) and entering the interior original sea water mixing in flash of steam chamber (32) through data feedback channel (6) (seawater overflow pipe), be flashed sea water pump (28) and extract out to be sent to and enter in the seawater flash pipe (26) after steam condensation chamber (33) is heated, participate in next flash distillation cyclic process.Because high temperature seawater, has reduced the fouling that steam condenser pipe (11) is gone up outer surface effectively not in the surperficial direct boiling of steam condenser pipe (11).
Claims (5)
1. integral type vaporizing liquid knockout drum device, by vaporization and condensation tank arrangement (1), heat exchange tank arrangement (2) composition that joins up and down, it is characterized in that vaporization and condensation tank arrangement (1) is last, heat exchange tank arrangement (2) is following, the tank body (3) of vaporization and condensation tank arrangement (1), the tank body (4) of heat exchange tank arrangement (2) be upright integral type vaporizing liquid knockout drum device tank body (5) on, hypomere, in tank body (5), be provided with liquid data feedback channel (6), liquid down going channel (7), the waiting of vaporization and condensation tank arrangement (1) the separating liquid input port of vaporizing communicates by liquid data feedback channel (6) with the cold fluid delivery outlet of heat exchange tank arrangement (2), the separating liquid of the vaporization delivery outlet of vaporization and condensation tank arrangement (1) communicates by liquid down going channel (7) with the hot fluid input port of heat exchange tank arrangement (2), has stoste cold fluid entrance (8) in the bottom of upright tank body (4), the hot fluid outlet (9) of having vaporized and having separated cooling.
2. integral type vaporizing liquid knockout drum device according to claim 1, it is characterized in that vaporization and condensation tank arrangement (1) is by tank body (3), steam condenser pipe (11), auxiliary heater (12), liquid-level switch sensor (13), blocking solution device (14), press steam turbine (15), press the steam absorbing tube (16) of steam turbine, press the steam pressing tube (17) of steam turbine to form, heat exchange tank arrangement (2) is by tank body (4), heat exchanger tube (18) is formed, have steam outlet (19) at the top of tank body (3), sidewall at tank body (3) has vapor inlet port (20), tank body (3) is divided into liquid data feedback channel (6) with the jar center section part of tank body (4) joint, the separating liquid of the vaporization output mouth of pipe of steam condenser pipe (11) and heat exchanger tube (18) the upper end hot fluid input mouth of pipe join, the pipe section of the hot fluid input mouth of pipe joint of the separating liquid of the vaporization output mouth of pipe of steam condenser pipe (11) and heat exchanger tube (18) is liquid down going channel (7), steam condenser pipe (11), auxiliary heater (12), liquid-level switch sensor (13), blocking solution device (14) is installed in the tank body (3), heat exchanger tube (18) is installed in the tank body (4), press steam turbine (15), steam absorbing tube (16), steam pressing tube (17) is installed on the tank body (3), steam absorbing tube (16) is connected with steam outlet (19), steam pressing tube (17) is connected with vapor inlet port (20), vapor inlet port (20) is connected with the steam inlet of steam condenser pipe (11), and heat exchanger tube (18) lower end cooling liquid outlet joins with the hot fluid outlet (9) that separates cooling of vaporizing of the bottom of tank body (4).
3. integral type vaporizing liquid knockout drum device according to claim 1, it is characterized in that vaporization and condensation tank arrangement (1) is by tank body (3), steam condenser pipe (11), auxiliary heater (12), liquid-level switch sensor (13), blocking solution device (14), press steam turbine (15), press the steam absorbing tube (16) of steam turbine, press the steam pressing tube (17) of steam turbine, strength of fluid probe (21) is formed, heat exchange tank arrangement (2) is by tank body (4), heat exchanger tube (18), concentrated liquid heat exchanger tube (22) is formed, being provided with a spacer assembly (23) in tank body (5) separates the interior sky of the interior sky of tank body (3) and tank body (4), liquid data feedback channel (6) is overflow lip on the liquid that spacer assembly (23) leaves, the upper end hot fluid input mouth of pipe of the separating liquid of the vaporization output mouth of pipe of steam condenser pipe (11) and heat exchanger tube (18) joins, the pipe section of the hot fluid input mouth of pipe joint, upper end of the separating liquid of the vaporization output mouth of pipe of steam condenser pipe (11) and heat exchanger tube (18) is liquid down going channel (7), have drain port under the concentrated liquid (24) at spacer assembly (23), have concentrated liquid outlet (25) in tank body (4) bottom, steam condenser pipe (11), auxiliary heater (12), liquid-level switch sensor (13), blocking solution device (14), strength of fluid probe (21) is installed in the tank body (3), heat exchanger tube (18), concentrated liquid heat exchanger tube (22) is installed in the tank body (4), press steam turbine (15), steam absorbing tube (16), steam pressing tube (17) is installed on the tank body (3), have steam outlet (19) at the top of tank body (3), sidewall at tank body (3) has vapor inlet port (20), steam absorbing tube (16) is connected with steam outlet (19), steam pressing tube (17) is connected with vapor inlet port (20), vapor inlet port (20) is connected with the steam inlet of steam condenser pipe (11), the lower end cooling liquid outlet of heat exchanger tube (18) separates the hot fluid outlet (9) of cooling off and joins with vaporizing of tank body (4) bottom, drain port (24) joins under the upper end liquid-inlet of concentrated liquid heat exchanger tube (22) and the concentrated liquid, and the concentrated liquid outlet (25) of the lower end liquid outlet of concentrated liquid heat exchanger tube (22) and tank body (4) bottom joins.
4. integral type vaporizing liquid knockout drum device according to claim 1, it is characterized in that vaporization and condensation tank arrangement (1) is by tank body (3), steam condenser pipe (11), auxiliary heater (12), liquid-level switch sensor (13), blocking solution device (14), press steam turbine (15), press the steam absorbing tube (16) of steam turbine, press the steam pressing tube (17) of steam turbine, strength of fluid probe (21), seawater flash pipe (26), flash boiling spray head unit (27), flash distillation sea water circulating pump (28), flash distillation sea water circulating pump suction hose (29), flash distillation sea water circulating pump pressure pipe (30) is formed, heat exchange tank arrangement (2) is by tank body (4), heat exchanger tube (18), concentrated liquid heat exchanger tube (22) is formed, being provided with a spacer assembly (23) in tank body (5) separates the interior sky of the interior sky of tank body (3) and tank body (4), in tank body (3), be provided with a flash distillation spacer assembly (31) in addition the interior sky of tank body (3) is divided into two parts up and down, top is flash of steam chamber (32), the bottom is steam condensation chamber (33), seawater flash pipe (26) is installed on the flash distillation spacer assembly (31), seawater flash pipe (26) lower end import is connected with the top of steam condensation chamber (33), the outlet of seawater flash pipe (26) upper end is connected with flash boiling spray head unit (27), being provided with seawater overflow pipe in tank body (5) is liquid data feedback channel (6), liquid data feedback channel (6) (seawater overflow pipe) passes steam condensation chamber (33), liquid data feedback channel (6) is gone up logical flash of steam chamber (32), the interior sky of following logical tank body (4), the separating liquid of the vaporization output mouth of pipe of steam condenser pipe (11) and heat exchanger tube (18) the upper end hot fluid input mouth of pipe join, the pipe section of the separating liquid of the vaporization output mouth of pipe of steam condenser pipe (11) and hot fluid input mouth of pipe joint, heat exchanger tube (18) upper end is liquid down going channel (7), in tank body (5), be provided with and let out pipe (34) under the concentrated seawater, letting out pipe (34) upper end under the concentrated seawater communicates with flash of steam chamber (32), letting out the upper end liquid-inlet that pipe (34) is passed down through its lower end, steam condensation chamber (33) back and concentrated liquid heat exchanger tube (22) under the concentrated seawater joins, lower sidewall in flash of steam chamber (32) has flash distillation seawer outlet (35), lower sidewall at steam condensation chamber (33) has flash distillation sea intake (36), have concentrated liquid outlet (25) in tank body (4) bottom, have steam outlet (19) at the top of tank body (3), sidewall at tank body (3) has vapor inlet port (20), steam condenser pipe (11) is installed in the steam condensation chamber (33), auxiliary heater (12) is installed on the seawater flash pipe (26), liquid-level switch sensor (13), blocking solution device (14), strength of fluid probe (21) is installed in the flash of steam chamber (32), heat exchanger tube (18), concentrated liquid heat exchanger tube (22) is installed in the tank body (4), press steam turbine (15), steam absorbing tube (16), steam pressing tube (17), flash distillation sea water circulating pump (28), flash distillation sea water circulating pump suction hose (29), flash distillation sea water circulating pump pressure pipe (30) is installed on the tank body (3), steam absorbing tube (16) is connected with steam outlet (19), steam pressing tube (17) is connected with vapor inlet port (20), vapor inlet port (20) is connected with the steam inlet of steam condenser pipe (11), the lower end cooling liquid outlet of heat exchanger tube (18) separates the hot fluid outlet (9) of cooling off and joins with vaporizing of the bottom of tank body (4), the concentrated liquid outlet (25) of the lower end liquid outlet of concentrated liquid heat exchanger tube (22) and tank body (4) bottom joins, flash distillation sea water circulating pump suction hose (29) joins with flash distillation seawer outlet (35), and flash distillation sea water circulating pump pressure pipe (30) joins with flash distillation sea intake (36).
5. according to claim 1,2,3,4 described integral type vaporizing liquid knockout drum devices, it is characterized in that having deslagging drain (10) in the bottom of tank body (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011104431582A CN103182194A (en) | 2011-12-27 | 2011-12-27 | Integrated-type liquid vaporization-separation tank device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011104431582A CN103182194A (en) | 2011-12-27 | 2011-12-27 | Integrated-type liquid vaporization-separation tank device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103182194A true CN103182194A (en) | 2013-07-03 |
Family
ID=48673791
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011104431582A Pending CN103182194A (en) | 2011-12-27 | 2011-12-27 | Integrated-type liquid vaporization-separation tank device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103182194A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109092100A (en) * | 2018-10-31 | 2018-12-28 | 无锡恒诚硅业有限公司 | A kind of residual neat recovering system of solid water glass dissolution |
| CN109762659A (en) * | 2019-01-31 | 2019-05-17 | 安徽省新洲海洋生物制品有限公司 | A kind of purifying tank of fish oil |
| CN111167144A (en) * | 2020-02-27 | 2020-05-19 | 中国华能集团清洁能源技术研究院有限公司 | Sectional condensation type desulfurization slurry flash evaporation heat extraction water taking device and method |
| CN114177638A (en) * | 2021-12-28 | 2022-03-15 | 东莞市恒建环保科技有限公司 | Single-steaming treatment process for copper sulfate mother liquor |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2098318U (en) * | 1991-05-26 | 1992-03-11 | 云南省曲靖地区第一人民医院 | High-efficiency film separation tower |
| CN201356986Y (en) * | 2008-11-03 | 2009-12-09 | 如皋市双马化工有限公司 | Self-circulation sweet water concentrator |
| CN101716422A (en) * | 2009-12-15 | 2010-06-02 | 广州市心德实业有限公司 | Integrated multistage climbing-film evaporator |
| WO2010089478A1 (en) * | 2009-02-04 | 2010-08-12 | Roland Laruelle | Distillation device with recovery of heat, using concentric tubes |
-
2011
- 2011-12-27 CN CN2011104431582A patent/CN103182194A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2098318U (en) * | 1991-05-26 | 1992-03-11 | 云南省曲靖地区第一人民医院 | High-efficiency film separation tower |
| CN201356986Y (en) * | 2008-11-03 | 2009-12-09 | 如皋市双马化工有限公司 | Self-circulation sweet water concentrator |
| WO2010089478A1 (en) * | 2009-02-04 | 2010-08-12 | Roland Laruelle | Distillation device with recovery of heat, using concentric tubes |
| CN101716422A (en) * | 2009-12-15 | 2010-06-02 | 广州市心德实业有限公司 | Integrated multistage climbing-film evaporator |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109092100A (en) * | 2018-10-31 | 2018-12-28 | 无锡恒诚硅业有限公司 | A kind of residual neat recovering system of solid water glass dissolution |
| CN109762659A (en) * | 2019-01-31 | 2019-05-17 | 安徽省新洲海洋生物制品有限公司 | A kind of purifying tank of fish oil |
| CN111167144A (en) * | 2020-02-27 | 2020-05-19 | 中国华能集团清洁能源技术研究院有限公司 | Sectional condensation type desulfurization slurry flash evaporation heat extraction water taking device and method |
| CN111167144B (en) * | 2020-02-27 | 2023-08-08 | 中国华能集团清洁能源技术研究院有限公司 | Device and method for flash evaporation extraction of hot water from desulfurization slurry by zone condensation |
| CN114177638A (en) * | 2021-12-28 | 2022-03-15 | 东莞市恒建环保科技有限公司 | Single-steaming treatment process for copper sulfate mother liquor |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203836931U (en) | Centralized-packing closed type high temperature steam condensate water recovery system | |
| CN205535749U (en) | Boiler -steam dome continuous blowdown water heat recovery system | |
| CN207507042U (en) | Multiple-effect falling film evaporator | |
| JP2015100724A5 (en) | ||
| CN105833555A (en) | Plate heat exchanger concentration system and concentration process thereof | |
| CN107008026A (en) | Nickel sulfate evaporative crystallization technique | |
| CN103182194A (en) | Integrated-type liquid vaporization-separation tank device | |
| CN102249203A (en) | Phosphoric acid evaporation process and device thereof | |
| CN207197285U (en) | A kind of on-condensible gas removal device | |
| CN109173309A (en) | A kind of MVR thermal concentration circulating and evaporating system | |
| CN104922921B (en) | A kind of self-loopa MVR thermo-compression evaporation systems | |
| CN101966396B (en) | Evaporation device | |
| CN1679731A (en) | Chinese medicine liquid vacuum concentrating process and apparatus thereof | |
| CN202892947U (en) | Integrated distillation device | |
| CN207418323U (en) | A kind of split type condensing unit | |
| CN204404134U (en) | Pure steam generator | |
| CN211133043U (en) | Rectifying column waste heat recovery device | |
| CN2778277Y (en) | Chinese medicinal liquor vacuum condensation equipment | |
| CN105423623B (en) | The sewage water heating heat pump of alternative large-scale heating boiler | |
| CN207532811U (en) | A kind of liquid heating evaporation enrichment facility | |
| CN205598682U (en) | Concentrated system of plate heat exchanger | |
| CN110393934A (en) | MVR circulating and evaporating system and method for evaporating | |
| CN108815869A (en) | Liquid-purifying device | |
| CN205627127U (en) | MVR triple -effect evaporator | |
| CN205164164U (en) | Tape unit tool vapor recompression's tertiary concentrated system of falling liquid film circulation evaporating in succession |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20130703 |