CN103331076B - The mass-and heat-transfer device that a kind of absorption tower and heat exchanger unite two into one and preparation method - Google Patents
The mass-and heat-transfer device that a kind of absorption tower and heat exchanger unite two into one and preparation method Download PDFInfo
- Publication number
- CN103331076B CN103331076B CN201210276548.XA CN201210276548A CN103331076B CN 103331076 B CN103331076 B CN 103331076B CN 201210276548 A CN201210276548 A CN 201210276548A CN 103331076 B CN103331076 B CN 103331076B
- Authority
- CN
- China
- Prior art keywords
- tube
- heat exchanger
- heat
- tube bank
- upper cover
- 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.)
- Expired - Fee Related
Links
Landscapes
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Abstract
The mass-and heat-transfer device that a kind of absorption tower and heat exchanger unite two into one and method of work are the gas discharging technology such as chemical industry, petrochemical industry, environmental protection, medicine, its structural relation is: be installed with upper cover on the top of tube bank, the front, top of upper cover there is gas vent, an absorbent inlet tube is installed on upper cover top; The side, upper end of tube bank is provided with cooling water inlet, the side, lower end of tube bank is provided with coolant outlet, the lower end opposite side of tube bank is provided with discharge outlet; In the bottom of tube bank 7, low head is installed, the side of low head is provided with gas feed, the bottom of low head is provided with liquid outlet; Being installed with by two pieces of tube sheets, five pieces of deflection plates in the centre of upper and lower two pieces of sieve plates is 1/4 breach, and between two pieces of tube sheets, be installed with several heat exchanger tube, heat exchanger tube is with equilateral triangle arrangement; The filler of filling Φ 1.5mm-2.0mm in heat exchanger tube.
Description
Technical field: the present invention relates to gas discharging technology, the mass-and heat-transfer device that especially a kind of absorption tower and heat exchanger unite two into one and the method for works such as chemical industry, petrochemical industry, environmental protection, medicine.
Background technology: in Chemical Manufacture, a large amount of ammonia cannot recycling completely, causing a large amount of ammonia gas is discharged in air with emptying, ammonia is a kind of toxic gas of colourless irritant foul odour, great pollution is caused to environment, also create a large amount of wastes, economic loss is serious.Due to factors such as design and structures, some tail gas absorbers, do not play the effect of absorption, especially when summer temp is high.Because the ammonia gas in tail gas will be released a large amount of heats when absorbing, and heat cannot be taken away in common absorption tower, makes the constant temperature in absorption tower increase, and reduces when temperature raises solubility, cannot absorb completely at all.
Summary of the invention: the object of this invention is to provide mass-and heat-transfer device and method of work that a kind of absorption tower and heat exchanger unite two into one, which overcome the shortcoming of original technology, the object of the present invention is achieved like this, it is by gas vent, absorbent inlet tube, shower nozzle, sieve plate, cooling water inlet, deflection plate, tube bank, coolant outlet, low head, liquid outlet, gas feed, tube sheet, discharge outlet, heat exchanger tube, upper cover, flange, filler is formed by connecting, on the top of tube bank, upper cover is installed, the front, top of upper cover there is gas vent, an absorbent inlet tube is installed on upper cover top, the side, upper end of tube bank is provided with cooling water inlet, the side, lower end of tube bank is provided with coolant outlet, the lower end opposite side of tube bank is provided with discharge outlet, in the bottom of tube bank 7, low head is installed, the side of low head is provided with gas feed, the bottom of low head is provided with liquid outlet.
In the bottom of absorbent inlet tube, shower nozzle is installed, and on absorbent inlet tube, flange is installed; Shower nozzle is the corrosion resistant plate of arc, and with square arrangement, hole count is multiple.
Shower nozzle be fixed wtih one piece of sieve plate below, tube bank be fixed wtih another block sieve plate below, porose on two pieces of sieve plates, hole is with equilateral triangle arrangement.
Being installed with by two pieces of tube sheets, five pieces of deflection plates in the centre of upper and lower two pieces of sieve plates is 1/4 breach, and between two pieces of tube sheets, be installed with several heat exchanger tube, heat exchanger tube is with equilateral triangle arrangement; The filler of filling Φ 1.5mm-2.0mm in heat exchanger tube.
During work, the present invention takes away heat by increasing heat-exchanging tube bundle, makes shower water can absorb ammonia in tail gas completely.Tail gas walks tube side from lower to upper by gas feed, and shower water also walks tube side from top to down from shower nozzle, after the ammonia in tail gas is absorbed by shower water in tube bank, is discharged and recycles, residual exhaust emptying by bottom; Must take away the heat of generation completely for ensureing to absorb, therefore recirculated water walks shell side, to be intake to coolant outlet water outlet, form circulation by cooling water inlet.
Meaning of the present invention is: the temperature 1, reducing this equipment, achieves the absorption of device to ammonia in tail gas, decreases the waste of ammonia, reduce production cost; 2, achieve the multipurpose on similar absorption tower, multi-state uses.Achieving ammonia in Chemical Manufacture tail gas cannot the present situation of recycling completely; 3, by increasing former tower height degree, tube bank and internals, realize different instructions for uses, can meet Production requirement, atmospheric environment have also been obtained very large improvement; 4, gas plant ammonia can better be solved with the irretrievable problem of exhaust emissions, for gas plant high load capacity long-term operation lays the first stone.
Accompanying drawing illustrates: Fig. 1 is the structural representation of the mass-and heat-transfer device that a kind of absorption tower and heat exchanger unite two into one, in figure 1, gas vent 2, absorbent inlet tube 3, shower nozzle 4, sieve plate 5, cooling water inlet 6, deflection plate 7, tube bank 8, coolant outlet 9, low head 10, liquid outlet 11, gas feed 12, tube sheet 13, discharge outlet 14, heat exchanger tube 15, upper cover 16, flange 17, filler
Detailed description of the invention: embodiment 1, the present invention are formed by connecting by gas vent 1, absorbent inlet tube 2, shower nozzle 3, sieve plate 4, cooling water inlet 5, deflection plate 6, tube bank 7, coolant outlet 8, low head 9, liquid outlet 10, gas feed 11, tube sheet 12, discharge outlet 13, heat exchanger tube 14, upper cover 15, flange 16, filler 17, on the top of tube bank 7, upper cover 15 is installed, the front, top of upper cover 15 there is gas vent 1, on upper cover 15 top, an absorbent inlet tube 2 is installed; The side, upper end of tube bank 7 is provided with cooling water inlet 5, the side, lower end of tube bank 7 is provided with coolant outlet 8, the lower end opposite side of tube bank 7 is provided with discharge outlet 13; In the bottom of tube bank 7, low head 9 is installed, the side of low head 9 is provided with gas feed 11, the bottom of low head 9 is provided with liquid outlet 10.
Embodiment 2, in the bottom of absorbent inlet tube 2, shower nozzle 3 is installed, and on absorbent inlet tube 2, flange 16 is installed; Shower nozzle 3 is the corrosion resistant plate of arc, and with square arrangement, hole count is multiple.
Embodiment 3, shower nozzle 3 be fixed wtih one piece of sieve plate 4 below, be fixed wtih another block sieve plate 4 below in tube bank 7, porose on two pieces of sieve plates 4, hole is with equilateral triangle arrangement.
Embodiment 4, to be installed with by two pieces of tube sheets, 12, five pieces of deflection plates 6 in the centre of upper and lower two pieces of sieve plates 4 be 1/4 breach, and between two pieces of tube sheets 12, be installed with several heat exchanger tube 14, heat exchanger tube 14 is with equilateral triangle arrangement; The filler 17 of filling Φ 1.5mm-2.0mm in heat exchanger tube 14.
Embodiment 5, method of work of the present invention are: taking away heat by increasing heat-exchanging tube bundle 7, making shower water can absorb ammonia in tail gas completely.Tail gas walks tube side from lower to upper by gas feed 11, and shower water also walks tube side from top to down from shower nozzle 3, after the ammonia in tail gas is absorbed by shower water in tube bank 7, is discharged and recycles, residual exhaust emptying by bottom; Must take away the heat of generation completely for ensureing to absorb, therefore recirculated water walks shell side, to be intake to coolant outlet 8 water outlet, form circulation by cooling water inlet 5.
Claims (1)
1. the mass-and heat-transfer device that unites two into one of an absorption tower and heat exchanger, it is by gas vent (1), absorbent inlet tube (2), shower nozzle (3), sieve plate (4), cooling water inlet (5), deflection plate (6), tube bank (7), coolant outlet (8), low head (9), liquid outlet (10), gas feed (11), tube sheet (12), discharge outlet (13), heat exchanger tube (14), upper cover (15), flange (16), filler (17) is formed by connecting, it is characterized in that: on the top of tube bank (7), upper cover (15) is installed, the front, top of upper cover (15) there is gas vent (1), an absorbent inlet tube (2) is installed on upper cover (15) top, the side, upper end of tube bank (7) is provided with cooling water inlet (5), the side, lower end of tube bank (7) is provided with coolant outlet (8), the lower end opposite side of tube bank (7) is provided with discharge outlet (13), in the bottom of tube bank (7), low head (9) is installed, the side of low head (9) is provided with gas feed (11), the bottom of low head (9) is provided with liquid outlet (10), in the bottom of absorbent inlet tube (2), shower nozzle (3) is installed, and on absorbent inlet tube (2), flange (16) is installed, the corrosion resistant plate that shower nozzle (3) is arc, the hole on shower nozzle is with square arrangement, and hole count is multiple, shower nozzle (3) be fixed wtih one piece of sieve plate (4) below, be fixed wtih another block sieve plate (4) below in tube bank (7), upper porose two pieces of sieve plates (4), hole is with equilateral triangle arrangement, be provided with in housing upper and lower sieve plate, on lower perforated plate, deflection plate, between two pieces of tube sheets (12), be installed with several heat exchanger tube (14), heat exchanger tube (14) is with equilateral triangle arrangement, the filler (17) of filling Φ 1.5mm-2.0mm in heat exchanger tube (14).
2. a kind of absorption tower and heat exchanger described in claim 1 unite two into one the method for work of mass-and heat-transfer device, it is characterized in that: take away heat by increasing heat-exchanging tube bundle (7), make shower water can absorb ammonia in tail gas completely; Tail gas walks tube side from lower to upper by gas feed (11), and shower water also walks tube side from top to down from shower nozzle (3), after the ammonia in tail gas is absorbed by shower water in tube bank (7), is discharged and recycles, residual exhaust emptying by bottom; For ensureing to absorb the heat must taking away generation completely, therefore recirculated water walks shell side, is intake to coolant outlet (8) water outlet by cooling water inlet (5), forms circulation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210276548.XA CN103331076B (en) | 2012-08-06 | 2012-08-06 | The mass-and heat-transfer device that a kind of absorption tower and heat exchanger unite two into one and preparation method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210276548.XA CN103331076B (en) | 2012-08-06 | 2012-08-06 | The mass-and heat-transfer device that a kind of absorption tower and heat exchanger unite two into one and preparation method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103331076A CN103331076A (en) | 2013-10-02 |
| CN103331076B true CN103331076B (en) | 2015-11-18 |
Family
ID=49239322
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210276548.XA Expired - Fee Related CN103331076B (en) | 2012-08-06 | 2012-08-06 | The mass-and heat-transfer device that a kind of absorption tower and heat exchanger unite two into one and preparation method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103331076B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108267043B (en) * | 2018-03-06 | 2023-09-19 | 中大空调集团有限公司 | Tube side water outlet side water discharging device of shell-and-tube heat exchanger of central air conditioner |
| CN109200767B (en) * | 2018-10-24 | 2024-06-11 | 东莞埃欧热能技术有限公司 | Ammonia gas absorbing device |
| CN109554299A (en) * | 2018-12-12 | 2019-04-02 | 大化集团有限责任公司 | Carbonate the application method of tail gas and carbonating column cooling water heat in algae or Bacteria Culture |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101791510A (en) * | 2010-04-14 | 2010-08-04 | 天津大学 | Film-falling absorption tower |
| CN201899898U (en) * | 2010-12-08 | 2011-07-20 | 湖北江钻天祥化工有限公司 | Exhaust gas treatment device for synthesis of trichlorosilane |
| CN203030165U (en) * | 2012-08-06 | 2013-07-03 | 河南省中原大化集团有限责任公司 | Absorption tower and heat exchanger combined mass and heat transfer device |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5665022B2 (en) * | 2010-03-31 | 2015-02-04 | 新日鉄住金エンジニアリング株式会社 | Carbon dioxide gas recovery device |
-
2012
- 2012-08-06 CN CN201210276548.XA patent/CN103331076B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101791510A (en) * | 2010-04-14 | 2010-08-04 | 天津大学 | Film-falling absorption tower |
| CN201899898U (en) * | 2010-12-08 | 2011-07-20 | 湖北江钻天祥化工有限公司 | Exhaust gas treatment device for synthesis of trichlorosilane |
| CN203030165U (en) * | 2012-08-06 | 2013-07-03 | 河南省中原大化集团有限责任公司 | Absorption tower and heat exchanger combined mass and heat transfer device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103331076A (en) | 2013-10-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103331076B (en) | The mass-and heat-transfer device that a kind of absorption tower and heat exchanger unite two into one and preparation method | |
| CN203687686U (en) | Biomass particle cooling device | |
| CN2844831Y (en) | Non-equidistant segmental baffle board heat exchangers | |
| CN203030165U (en) | Absorption tower and heat exchanger combined mass and heat transfer device | |
| CN204787965U (en) | Gaseous strip heat exchanger of energy -efficient methyl alcohol | |
| CN203355524U (en) | Spray tower | |
| CN202132963U (en) | Heat boiler flue gas reclaiming device | |
| CN102166430A (en) | Method and device for flue gas desulfurization and desorption | |
| CN205066509U (en) | Energy -saving boiler flue gas heat reclamation device | |
| CN202270465U (en) | Combined device for absorbing acid gas | |
| CN202267076U (en) | Waste heat recovery device for tail gas of boiler | |
| CN202382598U (en) | Total heat type heat absorbing tower | |
| CN102679769A (en) | Novel tubular cooling device | |
| CN208275039U (en) | Water cooling coagulating type demister unit | |
| CN203024627U (en) | Round pore plate lean solvent cooler | |
| CN103170153A (en) | Toluene condenser | |
| CN206881463U (en) | Vacuum tail gas cools down absorption recycling device | |
| CN203108250U (en) | Negative-pressure moisture separator | |
| CN204286171U (en) | Boiler heat-exchanger | |
| CN201382400Y (en) | Boiler heat exchanger | |
| CN102997710A (en) | Square counter flow type cooling tower | |
| CN205878965U (en) | Tail gas heat transfer device | |
| CN201221759Y (en) | Device for cooling ash | |
| CN205537189U (en) | Environment -friendly machine power ventilating and cooling tower of low running cost | |
| CN203108249U (en) | Double-layer condensing coil type steam-water separator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151118 Termination date: 20170806 |