CN1214320A - Scale-less waste water evaporating and concentrating process - Google Patents
Scale-less waste water evaporating and concentrating process Download PDFInfo
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- CN1214320A CN1214320A CN 98119049 CN98119049A CN1214320A CN 1214320 A CN1214320 A CN 1214320A CN 98119049 CN98119049 CN 98119049 CN 98119049 A CN98119049 A CN 98119049A CN 1214320 A CN1214320 A CN 1214320A
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Abstract
Indirect heating evaporator and contact heating evaporator are connected serially. The indirect heating evaporator is used when the concentration is low and the contact heating evaporator is used when the concentration is high. The present invention is named "indirect heating plus contact heating" evaporating and concentrating process. The said process has less scaling tendency and is saving in steam, water, power, and service cost.
Description
The present invention relates to a kind of evaporation technique, belong to evaporating and concentrating process.
Known evaporating and concentrating process, the normal method that adopts has two classes, and a class is the dividing wall type heating vaporization, as jacketed type vaporizer, pepe coil type evaporator, shell and tube evaporator etc.In wastewater treatment, the normal multiple-effect evaporator that adopts is a kind of typical shell and tube evaporator.This class vaporizer, maximum shortcoming are foulings easily on tube wall, and particularly when strength of solution was higher, fouling was more serious, influenced heat transfer property; Next is to use steam-heated cal(l)andria, and heat energy consumption is big; Also need to consume a large amount of water coolants.Another kind of is the contact heating vaporization, as submerged combustion evaporator, is that fuel and air are introduced the combustion chambers burn that is immersed in the solution, produces high-temperature flue gas, makes solution intensive bubbling and ebuillition of heated evaporation concentration.This class vaporizer, though there is not the partition heat-transfer surface, no scale problems will consume a large amount of fuel oils or combustion gas, process cost is very big.
The purpose of this invention is to provide a kind of technology that fouling tendency is little, energy consumption is low and be specially adapted to the waste water evaporation concentration that has.
The objective of the invention is to reach by following process technology scheme, it is characterized in that making dividing wall type heating fumigators and contact heating fumigators front and back series combination, when concentration is low, adopt the dividing wall type heating fumigators, when concentration is higher, adopt the contact heating fumigators.This technology can be called " heating of dividing wall type heating+contact " evaporating and concentrating process stream.
Scale-less effluents evaporating concentration process of the present invention is compared with existing processes, has following advantage:
1, adopt the dividing wall type heating vaporization when concentration is low, fouling tendency is less;
2, when concentration is higher, adopt the contact heating vaporization,, thoroughly eliminated the scale problems of heat-transfer surface owing to no partition hot face.Therefore, the dividing wall type heating vaporization can be called " not having the dirt evaporation ".
3, in the contact heating vaporization, do not need cooling system, saved a large amount of cooling waters.
4, in the contact heating vaporization, can utilize the used heat of stack gas, without steam,, saved effective energy without fuel oil or combustion gas.
5, combine and process cost low, can effectively save expenses such as vapour, water, electricity and Maintenance and Repair.
The invention will be further described below in conjunction with drawings and Examples.
Fig. 1 is " heating of dividing wall type heating+contact " of the present invention evaporating and concentrating process schema.
Fig. 2 is " multistage flash evaporation+nothing dirt evaporation " of the present invention evaporating and concentrating process flow process.
Fig. 3 is " multiple-effect evaporation+nothing dirt evaporation " of the present invention evaporating and concentrating process flow process.
Referring to Fig. 1, raw wastewater (3) enters dividing wall type heating fumigators (1), obtain than strong solution (4) through preliminary concentrating, strong solution (4) enters contact heating fumigators (2) and obtains final strong solution (5) through further concentrating, and strong solution (5) is discharged by the bottom of contact heating fumigators (2).
Referring to Fig. 2, raw wastewater (3) enters multistage flash distillation device (being the dividing wall type heating fumigators) (1), through the preheating of heat extraction section, be mixed into the further preheating of heat-recovery section with circulation fluid (6), reach top temperature through outer well heater (13) by giving birth to steam-heated cal(l)andria again, enter flashing chamber flash concentration step by step, after preliminary concentrating, draw from final stage, a part is mixed into the heat-recovery section preheating as the raw wastewater (3) after circulation fluid (6) and the preheating, a part enters no dirty vaporizer (both contact heating fumigators) (2) as strong solution (4), obtain final strong solution (5) through further concentrating, strong solution (5) is discharged by the bottom of no dirty vaporizer (2).In multistage flash distillation device (1), water of condensation at different levels (8) accumulates discharge step by step; Water coolant (9) is discharged in heat extraction section heat absorption back: non-condensable gases (10) is extracted out by vacuum pump by trails at different levels.In no dirty vaporizer (2), the part of strong solution (5) enters no dirty vaporizer (2) as circulation fluid (7) and mixes evaporation with concentrated solution (4) the spray atomizing that comes from multistage flash distillation device (1); The flow that also can make circulation fluid (7) is zero, and this is a special case of present embodiment; Stack gas (11) enters no dirty vaporizer (2) and evaporated liquor transmission of heat by contact, decreasing temperature and increasing humidity after gas-liquid separator (16) discharge as vent gas (12).
Referring to Fig. 3, raw wastewater (3) enters first single-effect evaporator (1-1) of multiple-effect evaporator (being the dividing wall type heating fumigators), obtain concentrated solution (4-1) through evaporation and enter second single-effect evaporator (1-2), obtain concentrated solution (4-2) through evaporation again and enter third effect evaporator (1-3), obtain concentrated solution (4-3) through evaporation again and enter third effect evaporator (1-3), obtain concentrated solution (4) through evaporation again and enter no dirty vaporizer (both contact heating fumigators) (2), obtain final strong solution (5) through further concentrating, strong solution (5) is discharged by the bottom of no dirty vaporizer (2).In multiple-effect evaporator, give birth to steam (17) and enter the evaporated liquor that first single-effect evaporator (1-1) heating first is imitated, the secondary steam (18) that evaporation produces enters the evaporated liquor that second single-effect evaporator (1-2) heating second is imitated, the secondary steam (19) that evaporation produces enters the evaporated liquor of third effect evaporator (1-3) heating triple effect, and the secondary steam (20) that evaporation produces is discharged condensation by condenser and discharged.In no dirty vaporizer (2), stack gas (11) enters no dirty vaporizer (2) and evaporated liquor transmission of heat by contact, discharges as vent gas (12) behind the decreasing temperature and increasing humidity.
Claims (2)
1, a kind of scale-less effluents evaporating concentration process is characterized in that making dividing wall type heating fumigators and contact heating fumigators front and back series combination, adopts the dividing wall type heating fumigators when concentration is low, adopts the contact heating fumigators when concentration is higher.
2, scale-less effluents evaporating concentration process according to claim 1, it is characterized in that its technology is " multistage flash evaporation+nothing dirt evaporation " evaporating and concentrating process flow process or " multiple-effect evaporation+nothings dirt evaporates " evaporating and concentrating process flow process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 98119049 CN1087002C (en) | 1998-10-12 | 1998-10-12 | Scale-less waste water evaporating and concentrating process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 98119049 CN1087002C (en) | 1998-10-12 | 1998-10-12 | Scale-less waste water evaporating and concentrating process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1214320A true CN1214320A (en) | 1999-04-21 |
| CN1087002C CN1087002C (en) | 2002-07-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 98119049 Expired - Fee Related CN1087002C (en) | 1998-10-12 | 1998-10-12 | Scale-less waste water evaporating and concentrating process |
Country Status (1)
| Country | Link |
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| CN (1) | CN1087002C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106044908A (en) * | 2016-06-29 | 2016-10-26 | 清华大学 | Evaporation treatment process of high-salinity organic waste water |
| CN106044905A (en) * | 2016-06-29 | 2016-10-26 | 清华大学 | Evaporation treatment system of high-salinity organic wastewater |
| CN108147608A (en) * | 2018-03-07 | 2018-06-12 | 华北电力大学（保定） | It is a kind of to utilize compressed air and the multiple-effect evaporation crystal system and method for heat pump treatment of Power brine waste |
-
1998
- 1998-10-12 CN CN 98119049 patent/CN1087002C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106044908A (en) * | 2016-06-29 | 2016-10-26 | 清华大学 | Evaporation treatment process of high-salinity organic waste water |
| CN106044905A (en) * | 2016-06-29 | 2016-10-26 | 清华大学 | Evaporation treatment system of high-salinity organic wastewater |
| CN108147608A (en) * | 2018-03-07 | 2018-06-12 | 华北电力大学（保定） | It is a kind of to utilize compressed air and the multiple-effect evaporation crystal system and method for heat pump treatment of Power brine waste |
| CN108147608B (en) * | 2018-03-07 | 2023-10-13 | 华北电力大学（保定） | Multi-effect evaporation crystallization system and method for treating power plant brine wastewater by using compressed air and heat pump |
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| Publication number | Publication date |
|---|---|
| CN1087002C (en) | 2002-07-03 |
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