CN215310251U - Single-effect concentrator single-condensation combined recovery device - Google Patents

Single-effect concentrator single-condensation combined recovery device Download PDF

Info

Publication number
CN215310251U
CN215310251U CN202121131324.0U CN202121131324U CN215310251U CN 215310251 U CN215310251 U CN 215310251U CN 202121131324 U CN202121131324 U CN 202121131324U CN 215310251 U CN215310251 U CN 215310251U
Authority
CN
China
Prior art keywords
ring
air inlet
air
evaporation chamber
air exhaust
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.)
Active
Application number
CN202121131324.0U
Other languages
Chinese (zh)
Inventor
陈敏炎
谢贞贞
陈耀华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fujian Leephick Biotechnology Co ltd
Original Assignee
Fujian Leephick Biotechnology Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fujian Leephick Biotechnology Co ltd filed Critical Fujian Leephick Biotechnology Co ltd
Priority to CN202121131324.0U priority Critical patent/CN215310251U/en
Application granted granted Critical
Publication of CN215310251U publication Critical patent/CN215310251U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The utility model provides a single-effect concentrator single-condensation combined recovery device, which comprises an evaporation chamber, a heater and a condenser, wherein the right side of the evaporation chamber is connected with the heater, and the left side of the evaporation chamber is connected with the condenser: the upper part of the evaporation chamber is provided with an air inlet ring and an air exhaust ring; the air exhaust ring is positioned above the air inlet ring; the air inlet ring is hollow and fixedly arranged around the inner wall of the evaporation chamber and is provided with an air inlet; the air pumping ring is hollow and fixedly arranged around the inner wall of the evaporation chamber, and is provided with an air outlet; the air inlet ring is communicated with the air exhaust ring through a booster pump; the utility model has the beneficial effects that: when the equipment works, no defoaming agent is needed to be added; gas is not required to be put into the bubble rising process to break vacuum and temporarily stop boiling so as to achieve the purpose of defoaming; this experiment is novel when keeping original taste, former each composition ratio, improves production efficiency, has reduced the energy consumption.

Description

Single-effect concentrator single-condensation combined recovery device
Technical Field
The utility model relates to a single-effect concentrator single-condensation combined recovery device.
Background
The single-effect concentrator single-condensation combined recovery device has the fundamental principle that dilute solution is heated to boil, so that part of moisture in the dilute solution is vaporized, and the aim of concentrating the solution is fulfilled; during the operation of the equipment, hot steam enters the shell pass of the heater, feed liquid enters the tube pass of the heater, the liquid level of the feed liquid rises after the feed liquid is heated, the feed liquid is sprayed into the evaporation chamber from the injection tube for vapor-liquid separation, the feed liquid in the evaporation chamber returns to the lower part of the heater from the circulating tube to be heated, the feed liquid is sprayed into the evaporation chamber again after being heated to form circulation, the feed liquid is contracted to a certain degree, and the feed liquid is discharged from the discharge port after being qualified after sampling; the upper steam enters the shell pass of the tubular condenser through vacuum pumping, is condensed into liquid by cooling water in the tube pass, enters a condensed water collecting tank and is discharged by a condensed water pump.
When steam is generated above the evaporation chamber, a plurality of foams are generated, when the foams are accumulated too high, the foams are pumped into the shell and tube condenser for cooling, the foams also contain effective components of substances, raw materials are wasted, and the cost is increased; there are two methods currently used: firstly, a defoaming agent is added in the process to achieve the purpose of defoaming, the defect that the taste is damaged in food processing is overcome, and the medicament needs to be strictly proportioned to keep the proportion of the original formula; secondly, the evaporation chamber is provided with a vacuum breaking device, when the foam is too high, a ball valve of the vacuum breaking device is opened to admit air, the vacuum environment in the evaporation chamber is broken, the boiling point is increased, and the defoaming effect is achieved.
SUMMERY OF THE UTILITY MODEL
The utility model aims to overcome the defects and provide a single-effect concentrator single-condensation combined recovery device.
The utility model adopts the following technical scheme:
the utility model provides a single-effect concentrator single condensation combination recovery unit, includes evaporating chamber, heater, condenser, the evaporating chamber right side is connected the heater, the evaporating chamber left side is connected the condenser: the upper part of the evaporation chamber is provided with an air inlet ring and an air exhaust ring; the air exhaust ring is positioned above the air inlet ring; the air inlet ring is hollow and fixedly arranged around the inner wall of the evaporation chamber and is provided with an air inlet; the air pumping ring is hollow and fixedly arranged around the inner wall of the evaporation chamber, and is provided with an air outlet; the air inlet ring is communicated with the air exhaust ring through a booster pump.
Preferably, the air inlet is formed by distributing a plurality of air inlets on the air inlet ring; the air outlet is formed by distributing a plurality of air exhaust holes on the air exhaust ring.
Preferably, the air inlet is an air inlet slit which is surrounded on the air inlet ring; the air outlet is an air exhaust slit which is surrounded on the air exhaust ring.
Preferably, the air inlet ring and the air exhaust ring are both made of stainless steel.
The utility model has the beneficial effects that: when the equipment works, no defoaming agent is needed to be added; gas is not required to be put into the bubble rising process to break vacuum and temporarily stop boiling so as to achieve the purpose of defoaming; this experiment is novel when keeping original taste, former each composition ratio, improves production efficiency, has reduced the energy consumption.
Drawings
Fig. 1 is an overall schematic view of the present invention.
FIG. 2 is a schematic view of the air intake ring of the present invention.
FIG. 3 is a schematic view of the extraction ring of the present invention.
Detailed Description
In order to make the purpose and technical solution of the present invention clearer, the present invention is further described with reference to the accompanying drawings and embodiments:
as shown in fig. 1 to fig. 3, the single-effect concentrator and single-condensation combined recovery device comprises an evaporation chamber 1, a heater 2 and a condenser 3, wherein the right side of the evaporation chamber 1 is connected with the heater 2, and the left side of the evaporation chamber 1 is connected with the condenser 3: the upper part of the evaporation chamber 1 is provided with an air inlet ring 4 and an air exhaust ring 5; the gas extraction ring 5 is positioned above the gas inlet ring 4; the air inlet ring 4 is hollow and fixedly arranged around the inner wall of the evaporation chamber 1 and is provided with an air inlet; the air extracting ring 5 is hollow and fixedly arranged around the inner wall of the evaporation chamber 1 and is provided with an air outlet; the air inlet ring 4 is communicated with the air pumping ring 5 through a booster pump 6.
Preferably, the air inlet is formed by distributing a plurality of air inlets on the air inlet ring 4; the air outlet is formed by distributing a plurality of air exhaust holes on the air exhaust ring 5.
Preferably, the air inlet is an air inlet slit which is surrounded on the air inlet ring 4; the air outlet is an air exhaust slit which is surrounded on the air exhaust ring 5.
Preferably, the air inlet ring 4 and the air exhaust ring 5 are made of stainless steel.
The principle of the utility model is as follows: in the operation process of the single-effect concentrator single condensation combined recovery device, hot steam generated by a boiler (not shown in the figure) enters the shell pass of the heater 2 through a steam pipeline 21, feed liquid enters the tube pass of the heater 2, the liquid level of the feed liquid rises after being heated, the feed liquid is sprayed into the evaporation chamber 1 from the injection pipe 22 for steam-liquid separation, the feed liquid in the evaporation chamber 1 returns to the lower part of the heater 2 from the circulating pipe 11 to be heated again, the feed liquid is sprayed into the evaporation chamber 1 again after being heated to form circulation, the circulation is contracted to a certain degree, and the feed liquid is discharged from a discharge port after being qualified through sampling; steam above the evaporation chamber enters the shell pass of the tubular condenser 2 by vacuumizing, is condensed into liquid by cooling water in the tube pass, enters a condensed water collecting tank and is discharged by a condensed water pump.
When the bubbles generated in the process approach or reach the height of the air inlet ring 4, because the booster pump 6 works, the horizontal gas (the inside is not really vacuum, and the inside in normal production is generally 0.02-0.06MPa) of the air pumping ring 5 is pumped in and is sprayed out from the air inlet ring 4, so that the air inlet ring 4 has an instant pressure difference horizontally, the instant pressure difference exceeds the critical value of the surface tension of the bubbles, the bubbles are broken, the bubbles cannot exceed the horizontal line of the air inlet ring 4, and the bubbles cannot be pumped into a condenser in the process of vacuum pumping; since only the local pressure difference at the level of the air inlet ring 4 is changed, the overall pressure value of the evaporation chamber is not changed, and the influence on the vapor-liquid separation is slight.
In the description of the present invention, it should be noted that the terms "upper", "lower", "inner", "outer", "front", "rear", "both ends", "one end", "the other end", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of describing the present invention and simplifying the description, but do not indicate or imply that the referred device or element must have a specific orientation, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted", "provided", "connected", and the like are to be construed broadly, such as "connected", which may be fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
The components adopted by the utility model are all universal standard components or components known by the technicians in the field, and the structure and the principle of the components can be known by the technicians through technical manuals or conventional experimental methods; for example, the specific structures and corresponding connection modes of the evaporation chamber, the heater and the condenser are known to those skilled in the art, and are not described herein.
The above description is only a preferred embodiment of the present invention, and is not intended to limit the technical scope of the present invention, so that any minor modifications, equivalent changes and modifications made to the above embodiments according to the technical spirit of the present invention still belong to the protection scope of the present invention.

Claims (4)

1. The utility model provides a single-effect concentrator single condensation combination recovery unit, includes evaporating chamber, heater, condenser, the evaporating chamber right side is connected the heater, the evaporating chamber left side is connected the condenser: the method is characterized in that:
the upper part of the evaporation chamber is provided with an air inlet ring and an air exhaust ring;
the air exhaust ring is positioned above the air inlet ring;
the air inlet ring is hollow and fixedly arranged around the inner wall of the evaporation chamber and is provided with an air inlet;
the air pumping ring is hollow and fixedly arranged around the inner wall of the evaporation chamber, and is provided with an air outlet;
the air inlet ring is communicated with the air exhaust ring through a booster pump.
2. The single-effect concentrator single-condensation combined recovery device of claim 1, wherein:
the air inlet is formed by distributing a plurality of air inlets on the air inlet ring;
the air outlet is formed by distributing a plurality of air exhaust holes on the air exhaust ring.
3. The single-effect concentrator single-condensation combined recovery device of claim 1, wherein:
the air inlet is an air inlet slit which is surrounded on the air inlet ring;
the air outlet is an air exhaust slit which is surrounded on the air exhaust ring.
4. The single-effect concentrator single-condensation combined recovery device according to any one of claims 1 to 3, characterized in that:
the air inlet ring and the air exhaust ring are both made of stainless steel.
CN202121131324.0U 2021-05-25 2021-05-25 Single-effect concentrator single-condensation combined recovery device Active CN215310251U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202121131324.0U CN215310251U (en) 2021-05-25 2021-05-25 Single-effect concentrator single-condensation combined recovery device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202121131324.0U CN215310251U (en) 2021-05-25 2021-05-25 Single-effect concentrator single-condensation combined recovery device

Publications (1)

Publication Number Publication Date
CN215310251U true CN215310251U (en) 2021-12-28

Family

ID=79548087

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202121131324.0U Active CN215310251U (en) 2021-05-25 2021-05-25 Single-effect concentrator single-condensation combined recovery device

Country Status (1)

Country Link
CN (1) CN215310251U (en)

Similar Documents

Publication Publication Date Title
CN100571836C (en) Device for extracting alcohol soluble plant component
CN215310251U (en) Single-effect concentrator single-condensation combined recovery device
CN202777833U (en) Mechanical vapor recompression evaporator
CN112093836A (en) Waste water heat pump type low-temperature evaporator
CN206995895U (en) MVR traditional Chinese drug inspissation systems with defoaming function
CN209333221U (en) A kind of single-effect external circulation inspissator
CN201182919Y (en) Device for extracting alcohol-soluble plant composition
CN213623353U (en) Waste water heat pump type low-temperature evaporator
CN211302117U (en) Vacuum concentration system utilizing refrigerant to directly condense and heat and tea juice concentrator
CN218853514U (en) Hot reflux extraction and concentration equipment
CN208785784U (en) A kind of external circulation evaporator
CN104864754A (en) Heat pipe type heat energy recovery device
CN206944741U (en) A kind of even distribution type multi-stage, efficient condensing unit
CN214714389U (en) Low-temperature vacuum evaporation device
CN214842588U (en) Multistage steam jet vacuum pumping system
CN219423748U (en) Improved heat exchanger for low-temperature evaporation equipment
CN216497501U (en) Vacuum multiple concentration system
CN211383819U (en) Vacuum concentration device and energy-saving efficient tea juice concentration system
CN212383235U (en) Energy-saving viscose deaeration steam sprays vacuum pumping system
CN211302107U (en) Energy-saving type low-concentration liquid vacuum concentration system
CN215327046U (en) Triple-effect waste water evaporator
CN211536563U (en) Traditional chinese medicine extract evaporation and concentration device
CN219156560U (en) Brewing wastewater low-temperature evaporation concentration system
CN204684685U (en) A kind of cryogenic vacuum Chinese medicinal concentration equipment
CN209816098U (en) Efficient low-alcoholization red wine and brandy making device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant