CN204503044U - Distillation cooling corollary system - Google Patents
Distillation cooling corollary system Download PDFInfo
- Publication number
- CN204503044U CN204503044U CN201520057745.1U CN201520057745U CN204503044U CN 204503044 U CN204503044 U CN 204503044U CN 201520057745 U CN201520057745 U CN 201520057745U CN 204503044 U CN204503044 U CN 204503044U
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- China
- Prior art keywords
- condenser
- stage
- pipeline
- secondary condenser
- hydrolysis kettle
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- 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.)
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The open a kind of distillation cooling corollary system of the utility model, this system comprises hydrolysis kettle, first-stage condenser, secondary condenser, dump tank, steam pipe, pipeline, valve.Hydrolysis kettle is connected with condenser by pipeline, connects secondary condenser after first-stage condenser by pipeline, and secondary condenser end is installed and is provided with dump tank.Connect steam pipe in the cooling liquid outlet end of first-stage condenser, secondary condenser end is connected with into condensate liquid inlet pipe.The utility model has the advantage of: the condenser in corollary equipment makes graphite condenser into by original PP modified graphite condenser effectively can prevent ageing equipment, prevents ageing equipment from leaking air.The blocking that material and incrustation scale assemble and cause in condenser is stopped at condenser cooling liquid outlet place access steam.Reduce labor strength, ensure normally to produce.
Description
Technical field
The utility model relates to field of chemical equipment, especially a kind of distillation cooling corollary system.
Background technology
Current hydrolysis post can produce a large amount of waste water and produce a large amount of heats when hydrolysis.And hydrolysis terminates rear needs waste water evaporate to dryness.When distilling, vapo(u)rizing temperature is higher, also can produce a large amount of heats.Containing a part of material of also mixing in hot gas.Direct discharge can cause larger environmental pollution, also wastes material simultaneously, increases production cost.Need first to carry out doing further absorption again after condensation through condenser.The graphite modified condenser of PP of one 3 square metres of the supporting employing of current device carries out condensation, in condensation process, easily assembles material in condenser, easily produces incrustation scale in coolant pipe.Use and cause blockage of condenser afterwards several times, system cannot normally work.And PP material is very easily aging by high temperature, cause condenser to break, gas is run out of, contaminated environment.Ordinary maintenance increases production cost to workshop, affects manufacturing schedule.And the material of assembling in condenser can not be recycled, and causes yield to decline.
Summary of the invention
The purpose of this utility model is to provide a kind of distillation cooling corollary system, and this system can effectively solve blockage of condenser problem, does not need to carry out dredging cleaning.
The technical solution of the utility model is: a kind of distillation cooling corollary system, this system comprises hydrolysis kettle, first-stage condenser, secondary condenser, dump tank, steam pipe, pipeline, valve.Hydrolysis kettle is connected with first-stage condenser by pipeline, and first-stage condenser connects secondary condenser by pipeline, and secondary condenser end is installed and is provided with dump tank.Connect steam pipe in the cooling liquid outlet end of condenser, secondary condenser end is connected with into condensate liquid inlet pipe.
The position of first-stage condenser and secondary condenser is higher than hydrolysis kettle, and the position of first-stage condenser is higher than secondary condenser.
First-stage condenser and secondary condenser adopt graphite condenser.
The utility model has the advantage of: the condenser in corollary equipment makes graphite condenser into by original PP modified graphite condenser effectively can prevent ageing equipment, prevents ageing equipment from leaking air.The blocking that material and incrustation scale assemble and cause in condenser is stopped at condenser cooling liquid outlet place access steam.Reduce labor strength, ensure normally to produce.
Accompanying drawing explanation
Fig. 1 is the utility model distillation cooling corollary system structural representation.
Detailed description of the invention
A kind of distillation cooling corollary system, this system comprises hydrolysis kettle 1, first-stage condenser 2, secondary condenser 3, dump tank 4, steam pipe 5, pipeline 6, valve 7.Hydrolysis kettle 1 is connected with first-stage condenser 2 by pipeline 6, and first-stage condenser 2 connects secondary condenser 3 by pipeline, and secondary condenser 3 end is installed and is provided with dump tank 4.Connect steam pipe 5 in the cooling liquid outlet end of first-stage condenser, secondary condenser end is connected with into condensate liquid inlet pipe 8.Distillation during operation in hydrolysis kettle is by condenser and secondary condenser cooling, condensed water is discharged after secondary condenser to first-stage condenser, each distillation terminates rear steam and cleans condenser, the steam of cleaning is discharged after first-stage condenser to secondary condenser, effectively stops the problem produced because of the blocking of condenser.
Claims (3)
1. a distillation cooling corollary system, is characterized in that: this system comprises hydrolysis kettle (1), first-stage condenser (2), secondary condenser (3), dump tank (4), steam pipe (5), pipeline (6), valve (7); Hydrolysis kettle is connected with first-stage condenser by pipeline (6), secondary condenser is connected by pipeline after first-stage condenser, secondary condenser end is installed and is provided with dump tank, connect steam pipe (5) in the cooling liquid outlet end of first-stage condenser, secondary condenser end is connected with into condensate liquid inlet pipe (8).
2. distillation cools corollary system according to claim 1, it is characterized in that: the position of first-stage condenser (2) and secondary condenser (3) is higher than hydrolysis kettle (1), and the position of first-stage condenser (2) is higher than secondary condenser (3).
3. distillation cools corollary system according to claim 1, it is characterized in that: first-stage condenser (2) and secondary condenser (3) adopt graphite condenser.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520057745.1U CN204503044U (en) | 2015-01-28 | 2015-01-28 | Distillation cooling corollary system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520057745.1U CN204503044U (en) | 2015-01-28 | 2015-01-28 | Distillation cooling corollary system |
Publications (1)
Publication Number | Publication Date |
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CN204503044U true CN204503044U (en) | 2015-07-29 |
Family
ID=53701048
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201520057745.1U Expired - Fee Related CN204503044U (en) | 2015-01-28 | 2015-01-28 | Distillation cooling corollary system |
Country Status (1)
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CN (1) | CN204503044U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107218809A (en) * | 2016-12-30 | 2017-09-29 | 郴州万墨环保科技有限公司 | A kind of many metal distillation temperature control condensed components evaporate single crude product vacuum drying oven |
-
2015
- 2015-01-28 CN CN201520057745.1U patent/CN204503044U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107218809A (en) * | 2016-12-30 | 2017-09-29 | 郴州万墨环保科技有限公司 | A kind of many metal distillation temperature control condensed components evaporate single crude product vacuum drying oven |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150729 Termination date: 20190128 |
|
CF01 | Termination of patent right due to non-payment of annual fee |