CN206514272U - The regeneration device of non-clean steam - Google Patents

The regeneration device of non-clean steam Download PDF

Info

Publication number
CN206514272U
CN206514272U CN201621390095.3U CN201621390095U CN206514272U CN 206514272 U CN206514272 U CN 206514272U CN 201621390095 U CN201621390095 U CN 201621390095U CN 206514272 U CN206514272 U CN 206514272U
Authority
CN
China
Prior art keywords
adapter
heat exchanger
inlet pipe
described device
water
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
CN201621390095.3U
Other languages
Chinese (zh)
Inventor
李金峰
姚战立
尚德敏
李伟
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.)
HIT (HARBIN INSTITUTE OF TECHNOLOGY) KINT TECHNOLOGY Co Ltd
Original Assignee
HIT (HARBIN INSTITUTE OF TECHNOLOGY) KINT TECHNOLOGY 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 HIT (HARBIN INSTITUTE OF TECHNOLOGY) KINT TECHNOLOGY Co Ltd filed Critical HIT (HARBIN INSTITUTE OF TECHNOLOGY) KINT TECHNOLOGY Co Ltd
Priority to CN201621390095.3U priority Critical patent/CN206514272U/en
Application granted granted Critical
Publication of CN206514272U publication Critical patent/CN206514272U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The regeneration device of non-clean steam, it is related to a kind of recycle device.One end of first adapter of the present utility model and the gas transmission end of First Heat Exchanger are connected, the other end is connected with the gas transmission end of the second heat exchanger, one end of second adapter and the water delivery end of First Heat Exchanger are connected, the other end is connected with water pump, one end of water inlet pipe is connected with water pump, the other end passes to cistern, one end of 3rd adapter is connected with the water delivery end of the second heat exchanger, the other end is connected with water inlet pipe, one end of 4th adapter and the discharge outlet of First Heat Exchanger are connected, the other end is passed to and blowoff basin, one end of 5th adapter is connected with vavuum pump, the other end is connected with the 4th adapter, one end of 6th adapter is connected with the second heat exchanger, the other end is connected with injector, the input of injector is connected with the 7th adapter, output end is connected with the 8th adapter, the output end of steam inlet pipe and the admission end of First Heat Exchanger are connected.The waste heat recovery that the utility model is used for during making wine.

Description

The regeneration device of non-clean steam
Technical field
The utility model is related to a kind of recycle device, and in particular to a kind of regeneration device of non-clean steam.
Background technology
During wine brewing, alcoholic workshop needs the cleaning steam of high temperature constant pressure without interruption, at this stage typically by Coal-fired steam boiler produces substantial amounts of steam to meet the environmental condition during alcoholic.At the same time, it can be produced during alcoholic The raw substantial amounts of non-clean steam of high temperature (i.e. corrosive high temperatures steam), existing alcoholic process is generally straight by the non-clean steam of high temperature Run in and put, that is, pollute environment again that can be slatterned using the waste heat reclaimed, cause the waste of energy, damage is also result in the energy Lose.The waste heat containing acid vapor of alcoholic workshop discharge is reclaimed using Transformation Principle, while reducing boiler supplying alcoholic workshop Steam is cleaned, therefore the present apparatus is that non-clean high-temperature steam waste heat recovery can be solved into problem of environmental pollution again.
Utility model content
The utility model is to solve directly to discharge the non-clean steam of high temperature during existing alcoholic so that waste heat can not Effectively utilize, the problem of causing environmental pollution.And a kind of regeneration device of non-clean steam is provided.
A kind of regeneration device of non-clean steam of the present utility model, it, which is constituted, includes First Heat Exchanger, second changes Hot device, injector, water pump, vavuum pump, cistern, first adapter, second adapter, the 3rd adapter, the 4th adapter, the 5th adapter, 6th adapter, the 7th adapter, the 8th adapter, water inlet pipe, blowoff basin, drainpipe and steam inlet pipe, one end and first of the first adapter Heat exchanger gas transmission end connection, first adapter the other end be connected with the gas transmission end of the second heat exchanger, second take over one end and The water delivery end connection of First Heat Exchanger, the other end of the second adapter is connected with water pump, and one end of water inlet pipe is connected with water pump, water inlet The other end of pipe passes to cistern, and one end of the 3rd adapter is connected with the water delivery end of the second heat exchanger, the other end of the 3rd adapter It is connected with water inlet pipe, one end of the 4th adapter and the discharge outlet of First Heat Exchanger are connected, and the other end of the 4th adapter is passed to and arranged Pond, one end of the 5th adapter is connected with vavuum pump, and the other end of the 5th adapter is connected with the 4th adapter, one end of the 6th adapter It is connected with the second heat exchanger, the other end of the 6th adapter is connected with injector, the input of injector is connected with the 7th adapter, is drawn The output end of emitter with the 8th adapter be connected, one end of drainpipe is connected with the water delivery end of the second heat exchanger, drainpipe it is another End is passed to and blowoff basin, and the output end of steam inlet pipe and the admission end of First Heat Exchanger are connected.
Further, described device also includes parallel transistor and butterfly valve, and parallel transistor is in parallel with injector, and one end of parallel transistor It is connected with the 7th adapter, the other end of parallel transistor is connected with the 8th adapter, and butterfly valve is arranged on parallel transistor.
Further, described device also includes several dynamic valves, and the first adapter, the second adapter, the 4th adapter, the 5th connect Dynamic valve is mounted on pipe, the 6th adapter, the 7th adapter, the 8th adapter, water inlet pipe and steam inlet pipe.
Further, described device also includes being mounted on several flowmeters, the 6th adapter, the 8th adapter and steam inlet pipe Flowmeter.
Further, described device also includes several pressure gauges, and First Heat Exchanger, the second heat exchanger and the 8th adapter are upper equal Pressure gauge is installed.
Further, described device also includes being respectively mounted in thermometer, First Heat Exchanger, the second heat exchanger and the 8th adapter There is thermometer.
Further, described device also includes being mounted on liquid on liquid level gauge, First Heat Exchanger and the second heat exchanger Position indicating gage.
The technical solution of the utility model has the advantages that:
First, the technology that the utility model is combined using flash distillation and injection is non-clean high-temperature steam recovery and reusing and recycling, solution The problem of waste heat of having determined waste and environmental pollution.
2nd, the recyclable heat 158KJ/d of the utility model device.
3rd, the utility model saves softened water.
4th, the available non-clean high-temperature steam amount of the utility model is 6t/d.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present utility model.
Embodiment
Embodiment one:Illustrate present embodiment with reference to Fig. 1, present embodiment is changed including First Heat Exchanger 1, second Hot device 2, injector 3, water pump 4, vavuum pump 5, cistern 6, the first adapter 7, the second adapter 8, the 3rd adapter 9, the 4th adapter 10, 5th adapter 11, the 6th adapter 12, the 7th adapter 13, the 8th adapter 14, water inlet pipe 15, blowoff basin 16, drainpipe 19 and enter vapour Pipe 20, one end of the first adapter 7 is connected with the gas transmission end of First Heat Exchanger 1, the other end of the first adapter 7 and the second heat exchanger 2 Gas transmission end connection, one end of the second adapter 8 is connected with the water delivery end of First Heat Exchanger 1, the other end and water pump of the second adapter 8 4 connections, one end of water inlet pipe 15 is connected with water pump 4, and the other end of water inlet pipe 15 passes to cistern 6, one end of the 3rd adapter 9 Be connected with the water delivery end of the second heat exchanger 2, the other end of the 3rd adapter 9 is connected with water inlet pipe 15, one end of the 4th adapter 10 with The discharge outlet connection of First Heat Exchanger 1, the other end of the 4th adapter 10 pass to blowoff basin 16, one end of the 5th adapter 11 and Vavuum pump 5 is connected, and the other end of the 5th adapter 11 is connected with the 4th adapter 10, one end of the 6th adapter 12 and the second heat exchanger 2 Connection, the other end of the 6th adapter 12 is connected with injector 3, and the input of injector 3 is connected with the 7th adapter 13, the 7th adapter 13 input is connected with coal-fired steam boiler room 18, and the output end of injector 3 is connected with the 8th adapter 14, the 8th adapter (14) Output end pass to alcoholic workshop 27, one end of drainpipe 19 is connected with the water delivery end of the second heat exchanger 2, drainpipe 19 it is another End passes to and is connected with blowoff basin 16, the output end of steam inlet pipe 20 with the admission end of First Heat Exchanger 1, the input of steam inlet pipe 20 and Alcoholic workshop 27 is connected.
Embodiment two:Illustrate present embodiment with reference to Fig. 1, present embodiment is different from embodiment one It is that it also increases and has parallel transistor 17 and butterfly valve 24, parallel transistor 17 is in parallel with injector 3, and one end of parallel transistor 17 and the 7th adapter 13 connections, the other end of parallel transistor 17 is connected with the 8th adapter 14, and butterfly valve 24 is arranged on parallel transistor 17.Other compositions and connection Relation is identical with embodiment one.
Embodiment three:Illustrate present embodiment with reference to Fig. 1, present embodiment and embodiment one or two are not Be that it also increases and has several dynamic valves 21, the first adapter 7, the second adapter 8, the 4th adapter 10, the 5th adapter the 11, the 6th connect Dynamic valve 21 is mounted on pipe 12, the 7th adapter 13, the 8th adapter 14, water inlet pipe 15 and steam inlet pipe 20.Other compositions and company Connect relation identical with embodiment one or two.
Embodiment four:Illustrate present embodiment with reference to Fig. 1, present embodiment is different from embodiment three It is that it also increases to have and is mounted on flowmeter 22 on several flowmeters 22, the 6th adapter 12, the 8th adapter 14 and steam inlet pipe 20. Other compositions and annexation are identical with embodiment three.
Embodiment five:Illustrate present embodiment with reference to Fig. 1, present embodiment and embodiment one, two or It, which also increases, unlike four several pressure gauges 23, is respectively mounted in First Heat Exchanger 1, the second heat exchanger 2 and the 8th adapter 14 There is pressure gauge 23.Other compositions and annexation are identical with embodiment one, two or four.
Embodiment six:Illustrate present embodiment with reference to Fig. 1, present embodiment is different from embodiment five It is that it also increases and has thermometer 25, thermometer 25 is mounted in First Heat Exchanger 1, the second heat exchanger 2 and the 8th adapter 14. Other compositions and annexation are identical with embodiment five.
Embodiment seven:Illustrate present embodiment with reference to Fig. 1, present embodiment is different from embodiment six It is that it also increases and has liquid level gauge 26, liquid level gauge 26 is mounted on the heat exchanger 2 of First Heat Exchanger 1 and second.It is other Composition and annexation are identical with embodiment six.
Operation principle of the present utility model:
(94 DEG C) of the acidic high-temperature steam come out from alcoholic workshop 27 enters First Heat Exchanger 1 and gone out with the second heat exchanger 2 The water come discharged after heat exchange condensation, is entered the second heat exchanger 2 from the vapor of heat exchanger 1 out by the first adapter 7, is passed through Become the steam of cleaning reproducible utilization after the injection of injector 3, the vapor for the HTHP that the steam comes out with boiler is mixed It is re-used afterwards into alcoholic workshop.

Claims (7)

1. a kind of regeneration device of non-clean steam, described device includes First Heat Exchanger (1), the second heat exchanger (2), drawn Emitter (3), water pump (4), vavuum pump (5), cistern (6), the first adapter (7), the second adapter (8), the 3rd adapter (9), the 4th Take over (10), the 5th adapter (11), the 6th adapter (12), the 7th adapter (13), the 8th adapter (14), water inlet pipe (15), draining Pond (16), drainpipe (19) and steam inlet pipe (20), one end of the first adapter (7) are connected with the gas transmission end of First Heat Exchanger (1), the The other end of one adapter (7) is connected with the gas transmission end of the second heat exchanger (2), one end of the second adapter (8) and First Heat Exchanger (1) Water delivery end connection, second adapter (8) the other end be connected with water pump (4), one end of water inlet pipe (15) is connected with water pump (4), The other end of water inlet pipe (15) passes to cistern (6), and one end of the 3rd adapter (9) is connected with the water delivery end of the second heat exchanger (2), The other end of 3rd adapter (9) is connected with water inlet pipe (15), one end of the 4th adapter (10) and the discharge outlet of First Heat Exchanger (1) Connection, the other end of the 4th adapter (10) is passed to be connected with blowoff basin (16), one end of the 5th adapter (11) with vavuum pump (5), The other end of 5th adapter (11) is connected with the 4th adapter (10), and one end of the 6th adapter (12) is connected with the second heat exchanger (2), The other end of 6th adapter (12) is connected with injector (3), and the input of injector (3) is connected with the 7th adapter (13), injection The output end of device (3) is connected with the 8th adapter (14), and one end of drainpipe (19) is connected with the water delivery end of the second heat exchanger (2), The other end of drainpipe (19) is passed to and blowoff basin (16), the output end of steam inlet pipe (20) and the admission end of First Heat Exchanger (1) Connection.
2. the regeneration device of non-clean steam according to claim 1, it is characterised in that:Described device is also included simultaneously Union (17) and butterfly valve (24), parallel transistor (17) are in parallel with injector (3), and one end of parallel transistor (17) and the 7th adapter (13) Connection, the other end of parallel transistor (17) is connected with the 8th adapter (14), and butterfly valve (24) is arranged on parallel transistor (17).
3. the regeneration device of non-clean steam according to claim 1 or 2, it is characterised in that:Described device is also wrapped Include several dynamic valves (21), the first adapter (7), the second adapter (8), the 4th adapter (10), the 5th adapter (11), the 6th adapter (12), it is mounted on dynamic valve (21) on the 7th adapter (13), the 8th adapter (14), water inlet pipe (15) and steam inlet pipe (20).
4. the regeneration device of non-clean steam according to claim 3, it is characterised in that:Described device also includes number Flowmeter (22) is mounted on individual flowmeter (22), the 6th adapter (12), the 8th adapter (14) and steam inlet pipe (20).
5. the regeneration device of the non-clean steam according to claim 1,2 or 4, it is characterised in that:Described device is also Including several pressure gauges (23), pressure gauge is mounted in First Heat Exchanger (1), the second heat exchanger (2) and the 8th adapter (14) (23)。
6. the regeneration device of non-clean steam according to claim 5, it is characterised in that:Described device also includes temperature Thermometer (25) is mounted in degree meter (25), First Heat Exchanger (1), the second heat exchanger (2) and the 8th adapter (14).
7. the regeneration device of non-clean steam according to claim 6, it is characterised in that:Described device also includes liquid Liquid level gauge (26) is mounted on position indicating gage (26), First Heat Exchanger (1) and the second heat exchanger (2).
CN201621390095.3U 2016-12-16 2016-12-16 The regeneration device of non-clean steam Active CN206514272U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621390095.3U CN206514272U (en) 2016-12-16 2016-12-16 The regeneration device of non-clean steam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621390095.3U CN206514272U (en) 2016-12-16 2016-12-16 The regeneration device of non-clean steam

Publications (1)

Publication Number Publication Date
CN206514272U true CN206514272U (en) 2017-09-22

Family

ID=59862544

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621390095.3U Active CN206514272U (en) 2016-12-16 2016-12-16 The regeneration device of non-clean steam

Country Status (1)

Country Link
CN (1) CN206514272U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106838853A (en) * 2016-12-16 2017-06-13 哈尔滨工大金涛科技股份有限公司 The regeneration device of non-clean steam

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106838853A (en) * 2016-12-16 2017-06-13 哈尔滨工大金涛科技股份有限公司 The regeneration device of non-clean steam

Similar Documents

Publication Publication Date Title
CN103673747A (en) Fast washing equipment for large-size heat exchangers and washing method
CN206514272U (en) The regeneration device of non-clean steam
CN102519300A (en) Method for chemically and circularly cleaning scale inside and outside pipes of evaporating tank and heater in the sugar factory
CN102230817A (en) Recycled two-phase flow flowmeter calibrating platform of wet steam
CN101886263B (en) Blowing corrosion machine and method for corrosion and cleaning
CN103982886A (en) Partial jet flow small circulating ratio pipe casing type high temperature waste heat steam boiler
CN106838853A (en) The regeneration device of non-clean steam
CN204934152U (en) Dairy products cleaning device on the spot
CN109269344B (en) Online chemical cleaning liquid preparation system
CN103851953B (en) Pipe heat exchanger independence low discharge cyclic chemical descaling method
CN108050882B (en) On-line cleaning method for titanium plate heat exchangers
CN203965273U (en) Slurry density of desulfurizing absorption column measurement mechanism
CN203964986U (en) Desulphurization system absorbing tower liquid-level measuring system
CN105363320B (en) A kind of new and effective dealcoholysis formaldehyde absorbing tower
CN206924711U (en) Blender back purge system
CN206601067U (en) Aerostatic press intercooler self-stripping unit
CN220871563U (en) Descaling facility of heat exchanger
CN207654923U (en) A kind of combination unit of alkali cleaning and biological removal voc
CN212778763U (en) Heat recovery system
CN104950081A (en) On-line cleaning rate test method and device for shell-and-tube heat exchanger
CN215387651U (en) Process condensate recovery device of refining device
CN204503044U (en) Distillation cooling corollary system
CN205781989U (en) A kind of spherical tank blow-off line
CN203419888U (en) Diesel and wax oil hydrogenation device hydrogen presenting system
CN213050456U (en) Bulk drug processing jar aftertreatment system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant