CN2554618Y - Pressure treatment reactor - Google Patents

Pressure treatment reactor Download PDF

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Publication number
CN2554618Y
CN2554618Y CN 02243448 CN02243448U CN2554618Y CN 2554618 Y CN2554618 Y CN 2554618Y CN 02243448 CN02243448 CN 02243448 CN 02243448 U CN02243448 U CN 02243448U CN 2554618 Y CN2554618 Y CN 2554618Y
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CN
China
Prior art keywords
reactor
cooling
condensation
pipe
temperature
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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.)
Expired - Lifetime
Application number
CN 02243448
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Chinese (zh)
Inventor
郭强
王文忠
张涛
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Beijing Purkinje General Instrument Co Ltd
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Beijing Purkinje General Instrument Co Ltd
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Priority to CN 02243448 priority Critical patent/CN2554618Y/en
Application granted granted Critical
Publication of CN2554618Y publication Critical patent/CN2554618Y/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model relates to a water quality online monitoring instrument, in particular to a pressure digestion reactor. A gas condensation chamber is arranged above the reactor and is suited in a cooling pipe, the cooling pipe is provided with a cooling water inlet opening and a cooling water outlet opening, a sample introduction pipe is arranged between the reactor and the gas condensation chamber, and a fluid discharge pipe is arranged in the reactor. The utility model greatly reduces the time of water sample digestion in the water quality monitoring process, the seal reaction for ten minutes under the temperature of 200 DEG C can attain the same oxidized effect as the reaction for two hours under the temperature of 146 DEG C in the standard method, and the actual COD value of sewage can be accurately measured.

Description

The pressure dispelling reactor
Technical field
The utility model relates to environment automatic on-line monitoring instrument device field, relates in particular to a kind of pressure dispelling reactor.
Background technology:
Chemical oxygen demand (COD) (Chemical Oxygen Demand) is a most important contamination index in the monitoring water environment, it can be in order to judge the relative content of reducing substances (mainly being organism) in the water body, effect for water quality monitoring and processing, it is an important parameters, for the improvement of water pollution control and quality of water environment provides foundation, the pressure dispelling reactor is the important component part of COD water quality on-line monitoring instrument device, reactor is the container of various liquid mixing heating, the reactor that opens wide heating is subjected to the influence of reaction solution and makes the temperature of backflow system generally not high, adopt under the normal pressure in the standard law (GB11914-89) and clear up, reaction conditions is 146 ℃ of following oxidations 2 hours, could be relatively near the actual value of sewage.If require heat time heating time short, under the situation, heating obviously is worthless to measurement result under the normal pressure really and accurately.Airtight heating has obtained application in chemico-analytic laboratory, but this technology is not applied in the COD automatic on-line monitoring instrument device.Because as a closed container, under heating condition, need to take into full account the maximum pressure that it can bear, under high-temperature condition, do not clear up organic problem fast and also there is a kind of device effectively to solve at present.
Summary of the invention
The utility model purpose is the pressure dispelling problem of reactor in COD automatic on-line monitoring instrument device that makes with glass material in order to solve.
The utility model provides a kind of pressure dispelling reactor, outer wall place at reactor is provided with heating source, the top of reactor is the condensation of gas chamber, reactor communicates with the condensation of gas chamber, this condensation of gas chamber is set in the cooling tube, and cooling tube is provided with cooling water intake and cooling water outlet, is provided with the sample introduction pipe between reactor and condensation of gas chamber, drain pipe is housed in the reactor, is equiped with temperature tester on the reactor outer wall.
We are according to the needs of real reaction condition, the pressure in the reactor is improved and be controlled in the 0.11-0.13MPa.Such reaction conditions can improve the temperature of reaction to 200 ℃ in the container, has shortened the time of clearing up water sample greatly, improves oxidation efficiency.In heating process, in order to guarantee safety, temperature in the reactor is infinitely increased, we in the upper design of reactor special water cooling plant, promptly at the peripheral suit of condensation of gas chamber one cooling tube, feed the chilled water that constantly flows in the cooling tube, when the hot gas that liquid produces in the reactor during heating constantly rises to condensation chamber, by ice-cold condensation locular wall cooling liquid, thereby the air pressure of the inside is controlled in the 0.13MPa, the continuous rising of pressure in the reactor when having avoided heating, because the pressure in the reactor has increased, make the temperature in the reactor reach as high as 200 ℃, under high like this temperature, making those may be in the critical organism of clearing up can nearly all be cleared up in the short time fully.
Advantage of the present utility model is, shortened the time of clearing up water sample in the water quality monitoring greatly, measurement data is accurate, can reach equal oxidation effectiveness in two hours 146 ℃ of reactions with standard law in 10 minutes 200 ℃ of lower seal reactions, the result of result who measures and standard law (GB-11914-89) is very close, thereby can measure the actual COD value of sewage accurately.Digestion process of the present utility model is in air-tight state, and the chlorion in the water is oxidized to chlorine, in case after reaching vapor liquid equilibrium, the chlorion in the water is just no longer oxidized, thereby has effectively suppressed the interference of chlorion.
Description of drawings
The utility model is described in further detail below in conjunction with drawings and Examples.
Accompanying drawing is the structural representation of the utility model pressure dispelling reactor.
Among the figure: 1. cooling tube, 2. reactor, 3. reactor outer wall, 4. gas condensation chamber, 5. sample introduction pipe, 6. cooling water outlet, 7. blow-down pipe, 8. cooling water intake, 9. sample introduction pipe, 10 drain pipes, 11. temperature tester
Embodiment
It shown in the accompanying drawing most preferred embodiment of the present utility model.The outer wall 3 of reactor is provided with heating source, and the condensation of gas chamber 4 of reactor 2 tops communicates with reactor 2, and the condensation of gas chamber is set in the cooling tube 1, and chilled water flows in cooling tube 1 by cooling water intake 8 and cooling water outlet 6.Be provided with the sample introduction pipe between reactor and gas cooling chamber, the sample introduction pipe can have a plurality of, as sample introduction pipe 5 among the figure and sample introduction pipe 9, drain pipe 10 is housed in the reactor.Top, condensation of gas chamber is provided with blow-down pipe 7, is equiped with temperature tester 11 on the reactor outer wall 3.
When using the utility model pressure dispelling reactor to measure sewage, reaction liquid is through sample introduction pipe 5, and sample introduction pipe 9 enters reactor 2, sealing sample introduction pipe 5, blow-down pipe 7, sample introduction pipe 9 and drain pipe 10.To the reactor heating, solution is in 2 li pressurized power reactions of reactor by reactor outer wall 3 for well heater.Temperature in the reactor constantly increases makes the liquid gasification enter condensation of gas chamber 4, the outer wall of gas cooling chamber 4 is full of chilled water, make the steam liquefaction that produces owing to heating in the reactor, reach the purpose of cooling, make the maximum temperature maintenance in the entire container certain simultaneously.The temperature tester 11 of reactor can be measured the fluid temperature in the reactor at any time.

Claims (2)

1, a kind of pressure dispelling reactor, outer wall place at reactor is provided with heating source, it is characterized in that: in the top of reactor (2) is condensation of gas chamber (4), reactor communicates with the condensation of gas chamber, this condensation of gas chamber is set in the cooling tube (1), cooling tube (1) is provided with cooling water intake (8) and cooling water outlet (6), is provided with the sample introduction pipe between reactor and gas cooling chamber, and drain pipe (10) is housed in the reactor.
2, pressure dispelling reactor according to claim 1 is characterized in that: top, condensation of gas chamber is provided with blow-down pipe (7), is equiped with temperature tester (11) on the reactor outer wall (3).
CN 02243448 2002-08-05 2002-08-05 Pressure treatment reactor Expired - Lifetime CN2554618Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 02243448 CN2554618Y (en) 2002-08-05 2002-08-05 Pressure treatment reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 02243448 CN2554618Y (en) 2002-08-05 2002-08-05 Pressure treatment reactor

Publications (1)

Publication Number Publication Date
CN2554618Y true CN2554618Y (en) 2003-06-04

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 02243448 Expired - Lifetime CN2554618Y (en) 2002-08-05 2002-08-05 Pressure treatment reactor

Country Status (1)

Country Link
CN (1) CN2554618Y (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102445377A (en) * 2011-09-13 2012-05-09 济南大陆机电股份有限公司 Fully-enclosed high-temperature low-pressure digestion device
CN104587696A (en) * 2015-02-02 2015-05-06 银川多贝科技有限公司 Square gas cooling tank
CN105403448A (en) * 2015-11-30 2016-03-16 江苏德林环保技术有限公司 COD open microtube digestion method and device
CN105473994A (en) * 2013-06-21 2016-04-06 7685297加拿大有限公司 Systems and methods for preparing samples for chemical analysis using a cooled digestion zone

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102445377A (en) * 2011-09-13 2012-05-09 济南大陆机电股份有限公司 Fully-enclosed high-temperature low-pressure digestion device
CN102445377B (en) * 2011-09-13 2015-08-12 济南大陆机电股份有限公司 A kind of totally-enclosed high-temperature low-pressure digestion device
CN105473994A (en) * 2013-06-21 2016-04-06 7685297加拿大有限公司 Systems and methods for preparing samples for chemical analysis using a cooled digestion zone
CN105473994B (en) * 2013-06-21 2019-03-08 7685297加拿大有限公司 System and method for using cooling resolution area to prepare chemical analysis sample
CN104587696A (en) * 2015-02-02 2015-05-06 银川多贝科技有限公司 Square gas cooling tank
CN105403448A (en) * 2015-11-30 2016-03-16 江苏德林环保技术有限公司 COD open microtube digestion method and device
CN105403448B (en) * 2015-11-30 2018-10-19 江苏德林环保技术有限公司 A kind of COD opening micro-pipe digestion procedure and device

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GR01 Patent grant
C17 Cessation of patent right
CX01 Expiry of patent term

Expiration termination date: 20120805

Granted publication date: 20030604