CN212039068U

CN212039068U - Movable energy-saving distillation system

Info

Publication number: CN212039068U
Application number: CN202020491438.5U
Authority: CN
Inventors: 何燕
Original assignee: Suzhou Hanhao Separation Technology Co ltd
Current assignee: Suzhou Hanhao Separation Technology Co ltd
Priority date: 2020-04-07
Filing date: 2020-04-07
Publication date: 2020-12-01
Anticipated expiration: 2030-04-07

Abstract

The utility model provides a portable energy-conserving distillation system, including falling film evaporator, condensing equipment, centrifuge and transfer pot, falling film evaporator's export with condensing equipment connects, condensing equipment with centrifuge connects, centrifuge and/or falling film evaporator with the transfer pot is connected. The utility model discloses a portable energy-conserving distillation system adopts the feed liquor to preheat the heat exchanger, and the low temperature of make full use of feed liquor and secondary steam's high temperature have both realized the intensification of feed liquor, save heat energy, have condensed partial secondary steam again, have saved the circulation volume of refrigerant, and with the cooperation of movable transfer pot, constitute complete portable small-size distillation system, have stronger place adaptability.

Description

Movable energy-saving distillation system

Technical Field

The utility model relates to a concentrated technical field of chemical industry, concretely relates to portable energy-conserving distillation system.

Background

The falling film evaporation is that the feed liquid is added from an upper pipe box of a heating chamber of the falling film evaporator, is uniformly distributed into each heat exchange pipe through a liquid distribution and film forming device, and flows from top to bottom in a uniform film shape under the action of gravity, vacuum induction and airflow. In the flowing process, the shell-pass heating medium is heated and vaporized, the generated steam and the liquid phase enter a separation chamber of the evaporator together, the steam and the liquid are fully separated, the steam enters a condenser for condensation (single-effect operation) or enters a next-effect evaporator as the heating medium, so that the multi-effect operation is realized, and the liquid phase is discharged from the separation chamber.

At present, most of falling-film evaporators on the market adopt direct feeding, direct electric heating or indirect heat supply of electric heating steam, and a condensation tower adopts one-stage or multi-stage cooling of circulating water. The process equipment has the following disadvantages:

(1) the energy consumption is high. The efficiency of the electric steam heating equipment is unstable, and a discontinuous operation mode wastes a large amount of heat energy for the condensation and reheating of the steam;

(2) circulating water is directly condensed, heat energy of secondary steam is not recovered, and the energy-saving function is not realized. The cooling temperature is higher, the efficiency is low, the flow of circulating water is large, and the occupied area of equipment is large;

(3) the higher condensation temperature leads the condensate temperature to be higher, the steam content of the extraction solvent in the non-condensable gas is high, and equipment needs to supplement a large amount of solvent to maintain the recycling, and is not beneficial to the explosion prevention of the system;

and the existing distillation system equipment is not movable, and the use site is limited.

Therefore, it is an urgent problem to design a movable energy-saving distillation system.

SUMMERY OF THE UTILITY MODEL

The utility model aims at providing a portable energy-conserving distillation system to solve among the prior art falling liquid film distillation system energy consumption low-usage, equipment can not remove, use the limited and explosive unsafe problem in place.

In order to achieve the above object, the utility model provides a portable energy-conserving distillation system, including falling film evaporator, condensing equipment 4, centrifuge 5 and transfer pot 7, the export of falling film evaporator with condensing equipment 4 is connected, condensing equipment 4 with centrifuge 5 connects, centrifuge 5 and/or falling film evaporator with transfer pot 7 connects.

Further, falling film evaporator includes distillation column 1, plate heat exchanger 2 and vacuum pump 3, and the charge-in pipeline passes through vacuum pump 3 with one side of plate heat exchanger 2 is connected, the opposite side of plate heat exchanger 2 pass through the pipeline with the top of distillation column 1 is connected, the distillation column bottom is equipped with the concentrate export, the upper portion of distillation column 1 still is equipped with the secondary steam pipeline, the secondary steam pipeline with plate heat exchanger 2 is connected.

Further, a heating device 6 is provided outside the distillation column 1.

Further, the plate heat exchanger 2 comprises three plate heat exchangers: one side of the first plate heat exchanger 21 is connected with a feeding pipeline, and the other side is connected with a secondary steam pipeline from the distillation tower 1; one side of the second plate heat exchanger 22 is connected with a pipeline from the first plate heat exchanger 21, and the other side is connected with the first buffer tank 15 through the vacuum pump 3; the third plate heat exchanger 23 is connected to the vacuum pump 3, and the condensate of the first buffer tank 15 is pumped to the third heat exchanger 23 by the vacuum pump 3.

Further, the falling film evaporator further comprises a second buffer tank 16, wherein one end of the second buffer tank 16 is connected with the first plate heat exchanger 21, and the other end is connected with the distillation tower 1.

Further, the plate heat exchanger 2 is a brazed plate heat exchanger.

Further, the vacuum pump 3 is a liquid ring vacuum pump.

Further, universal rollers are mounted at the bottoms of the falling film evaporator, the centrifuge 5 and the transfer tank 7.

The movable energy-saving distillation system has the following advantages:

1. the utility model discloses a heat exchanger is preheated to the feed liquor, and the low temperature of make full use of feed liquor and secondary steam's high temperature have both realized the intensification of feed liquor, save heat energy, have condensed partial secondary steam again, have saved the circulation volume of refrigerant.

2. The liquid ring vacuum pump is used as a power source of the system, replaces a liquid inlet pump, a liquid outlet pump, a transfer pump and the like of the traditional equipment, and realizes the simplified design of the system.

3. The brazed plate type heat exchanger is adopted to replace a coil pipe and a shell and tube condenser, so that the heat transfer efficiency is higher, the equipment size is small, the integrated assembly is more suitable, and the maintenance and the operation are convenient.

4. And the movable small distillation system is matched with a movable transfer tank to form a complete movable small distillation system, and has stronger site adaptability.

Drawings

FIG. 1 is a schematic diagram of the movable energy-saving distillation system of the present invention;

fig. 2 is a schematic perspective view of the falling film evaporator of the present invention;

fig. 3 is a front view of the falling film evaporator of the present invention;

figure 4 is a right side view of the falling film evaporator of the present invention;

the device comprises a distillation tower 1, a distillation tower 2, a plate heat exchanger 21, a first plate heat exchanger 22, a second plate heat exchanger 23, a third plate heat exchanger 3, a vacuum pump 4, a cooling device 5, a centrifuge 6, a heating device 7, a transfer tank 7, a solvent transfer tank after extraction 7a, a crude oil transfer tank 7b, a CBD crude oil transfer tank 7c, a solvent recovery transfer tank 7d, a purified solvent transfer tank 7e, a solvent transfer tank after extraction 8, a filter 9, a console 15, a first buffer tank 16, a second buffer tank

Detailed Description

The present invention will be described in detail below with reference to embodiments shown in the drawings. However, these embodiments are not intended to limit the present invention, and structural, methodical, or functional changes that may be made by one of ordinary skill in the art based on these embodiments are all included in the scope of the present invention.

Terms such as "upper," "above," "lower," "below," and the like, used herein to denote relative spatial positions, are used for ease of description to describe one element or feature's relationship to another element or feature as illustrated in the figures. The spatially relative positional terms may be intended to encompass different orientations of the device in use or operation in addition to the orientation depicted in the figures. For example, if the device in the figures is turned over, elements described as "below" or "beneath" other elements or features would then be oriented "above" the other elements or features. Thus, the exemplary term "below" can encompass both an orientation of above and below. The device may be otherwise oriented (rotated 90 degrees or at other orientations) and the spatially relative descriptors used herein interpreted accordingly.

Also, it should be understood that, although the terms first, second, etc. may be used herein to describe various elements or structures, these described elements should not be limited by these terms. These terms are only used to distinguish these descriptive objects from one another. For example, the first plate heat exchanger may be referred to as a second plate heat exchanger, and similarly the second plate heat exchanger may also be referred to as a first plate heat exchanger, without departing from the scope of protection of the present application.

As shown in figures 1 and 2, the utility model provides a portable energy-conserving distillation system, including distillation column 1, plate heat exchanger 2, vacuum pump 3, condensing equipment 4, centrifuge 5 and transit tank 7. The feeding gets into plate heat exchanger 2 under vacuum pump 3's effect, get into the top of distillation column 1 after preheating of plate heat exchanger 2, the conduction oil heating in heating device 6 under the action of gravity, realize the evaporation in falling liquid film tube array, concentrate to the finished product, the finished product is collected to transfer jar 7b by the concentrate export, and steam in the distillation column 1 then gets into plate heat exchanger 2 once more through the secondary steam pipeline, so circulate, the intensification of feed liquor has both been realized, save heat energy, part secondary steam has condensed again, the circulation volume of refrigerant has been saved.

And a part of steam discharged from the plate heat exchanger 2 enters a centrifuge 5 for further separation, a part of steam enters the centrifuge 5 after being condensed by a cooling device 4, the extracted solvent is collected by a transfer tank 7a after being separated by the centrifuge 5, and the recovered solvent enters a transfer tank 7 c.

The vacuum pump 3 extracts the finished product CBD crude oil from the transfer tank 7b to the centrifuge 5 for further separation and purification, the obtained purified solvent is collected to the transfer tank 7d, the extracted solvent is collected to the transfer tank 7e, the extracted solvent is pumped to the centrifuge 5 through the vacuum pump 3 for further separation, the purified solvent is sent to the transfer tank 7d, the extracted solvent is collected to the transfer tank 7e, and the steps are repeated so as to further purify and separate the extracted solvent.

The universal rollers are arranged at the bottoms of the falling film evaporator, the centrifugal machine 5 and the transfer tank 7, so that a complete movable small distillation system is formed, and the device has stronger site adaptability.

As shown in FIGS. 2-4, the falling film evaporator of the movable energy-saving distillation system of the present invention comprises three plate heat exchangers, a distillation tower 1, a liquid ring vacuum pump 3 and a console 9, wherein the console 9 is used for controlling the vacuum pump 3 and the distillation tower 1. The feed liquor enters the first plate heat exchanger 21 through the filter 8 under the action of the liquid ring vacuum pump 3, enters the top of the distillation tower 1 after being preheated by the first plate heat exchanger 21, is heated by the heat conduction oil in the heating device 6 under the action of gravity, is evaporated in the falling film tube, and is concentrated to a finished product, the finished product is collected by a concentrated solution outlet, and the steam in the distillation tower 1 enters the first plate heat exchanger 21 again through a secondary steam pipeline.

A second buffer tank 16 is connected between the first plate heat exchanger 21 and the distillation column 1, and the second buffer tank 16 can be used for buffering steam and preventing the steam from carrying away products. The ejection of compact pipeline that comes out from first plate heat exchanger 21 is connected to one side of second plate heat exchanger 22, and the opposite side is connected to the extraction opening of vacuum pump 3, and first buffer tank 15 is connected to the gas vent of vacuum pump 3, and first buffer tank 15 is used for the primary separation of gas-liquid and provides the working solution for vacuum pump 3. The second plate heat exchanger is also connected with a condensing device through a cooling pipeline, and cooling liquid enters the second plate heat exchanger through the cooling pipeline to perform heat exchange treatment. Then the gas-liquid in the first buffer tank 15 is pumped to the third plate heat exchanger 23 by the vacuum pump 3, further condensed and finally discharged to a recycling port.

The liquid discharged from the third plate heat exchanger 23 may be further separated by a part of the centrifuge 5, a part of the liquid may be condensed by the cooling device 4 and then introduced into the centrifuge 5, the extracted solvent may be collected by the transfer tank 7a after separation by the centrifuge 5, and the recovered solvent may be introduced into the transfer tank 7 c. The vacuum pump 3 extracts the CBD crude oil from the transfer tank 7b to the centrifuge 5 for further separation and purification, the obtained purified solvent is collected to the transfer tank 7d, the extracted solvent is collected to the transfer tank 7e, the extracted solvent is pumped to the centrifuge 5 through the vacuum pump 3 for further separation, the purified solvent is sent to the transfer tank 7d, the extracted solvent is collected to the transfer tank 7e, and the steps are repeated in this way for further purification and separation.

The plate heat exchanger 2 is a brazed plate heat exchanger. The brazed plate type heat exchanger is adopted to replace a coil pipe and a shell and tube condenser, so that the heat transfer efficiency is higher, the equipment size is small, the integrated assembly is more suitable, and the maintenance and the operation are convenient.

Foretell vacuum pump 3 adopts liquid ring vacuum pump as the power source of system for liquid ring vacuum pump, replaces the feed liquor pump of traditional equipment, goes out the liquid pump, transfer pump etc. has realized the brief design of system.

The utility model discloses a distillation column 1's top is equipped with the manometer for control tower internal pressure, first plate heat exchanger 21 with be provided with the flowmeter on the connecting tube of distillation column 4 for control feeding velocity of flow. The falling film evaporator of the utility model can realize the total material flow rate of 250L/hr and the total evaporation rate of 250/hr.

It should be noted that the above-mentioned embodiments are only for the purpose of illustrating the preferred embodiments of the present invention, and are not intended to limit the present invention in any way, so that any modification or change of the present invention, which is made under the spirit of the same invention, should be included in the scope of the present invention.

Claims

1. A movable energy-saving distillation system is characterized by comprising a falling-film evaporator, a condensing device (4), a centrifugal machine (5) and a transfer tank (7), wherein the outlet of the falling-film evaporator is connected with the condensing device (4), the condensing device (4) is connected with the centrifugal machine (5), and the centrifugal machine (5) and/or the falling-film evaporator is connected with the transfer tank (7).

2. The movable energy-saving distillation system according to claim 1, wherein the falling film evaporator comprises a distillation tower (1), a plate heat exchanger (2) and a vacuum pump (3), a feeding pipeline is connected with one side of the plate heat exchanger (2) through the vacuum pump (3), the other side of the plate heat exchanger (2) is connected with the top of the distillation tower (1) through a pipeline, a concentrated solution outlet is arranged at the bottom of the distillation tower, a secondary steam pipeline is further arranged at the upper part of the distillation tower (1), and the secondary steam pipeline is connected with the plate heat exchanger (2).

3. Mobile energy saving distillation system according to claim 2, characterized in that the distillation column (1) is provided with heating means (6) on the outside.

4. A mobile energy saving distillation system according to claim 2, wherein the plate heat exchanger (2) comprises three plate heat exchangers: one side of the first plate heat exchanger (21) is connected with a feeding pipeline, and the other side of the first plate heat exchanger is connected with a secondary steam pipeline from the distillation tower (1); one side of the second plate heat exchanger (22) is connected with a pipeline coming out of the first plate heat exchanger (21), and the other side of the second plate heat exchanger is connected with the first buffer tank (15) through the vacuum pump (3); the third plate heat exchanger (23) is connected with the vacuum pump (3), and condensate of the first buffer tank (15) is pumped to the third plate heat exchanger (23) through the vacuum pump (3).

5. Mobile energy saving distillation system according to claim 4, characterized in that the falling film evaporator further comprises a second buffer tank (16), one end of the second buffer tank (16) being connected to the first plate heat exchanger (21) and the other end being connected to the distillation column (1).

6. A mobile energy saving distillation system according to claim 2, wherein the plate heat exchanger (2) is a brazed plate heat exchanger.

7. A mobile energy saving distillation system according to claim 2, characterized in that the vacuum pump (3) is a liquid ring vacuum pump.

8. The mobile energy saving distillation system according to claim 1, wherein the bottom of the falling film evaporator, centrifuge (5) and the transfer pot (7) are equipped with universal rollers.