CS272000B1 - A method of treating sludge wastewater from wet scrubbers and apparatus for its operation - Google Patents
A method of treating sludge wastewater from wet scrubbers and apparatus for its operation Download PDFInfo
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- CS272000B1 CS272000B1 CS873315A CS331587A CS272000B1 CS 272000 B1 CS272000 B1 CS 272000B1 CS 873315 A CS873315 A CS 873315A CS 331587 A CS331587 A CS 331587A CS 272000 B1 CS272000 B1 CS 272000B1
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Abstract
Cčelom spósobu spracovania sušpenzných odpadných vód z mokrých pračiek, vznikajúcich pri mokrom oolúčeni pevnej fázy z plynu Je dosiahnutie uzavretého vypieracieho okruhu. Z prúdu suspenzných - odpadných vód z prania sa oddelia nerozpustné částice a vyčištěné odpadné vody sa vracajú spát na pranie. Spósob sa prevádza na zariadení, kde za mokrou pračkou a pomocnou nádržkou Ja zaradený separátor například lamelový usadzovák alebo odstředivka, ktorý Ja spojený eo zásobníkom čirých vó»d a rscirkulač.ným čerpadlom.„Uplatnenie epóeobu β zariadenia umožňuje ziskanie vysoko zahusteI ného suapanznóho roztoku soli z mokrých. pračiek lepáim využitím vlaetného nizkopotencionálneho odpadného tepla prašných exhalátov bez nebezpečia zanášania, í resp. upchatia privodných tráe, trysiek a stáži pračiek, čim okrem zvýšenia pre-. vádzkovej istoty 9a vytváratpředpoklad vzniku bezodpadovaj technologie na technologických uzloch vyplsrania prašných exhalátov na mokrých pračkách.The aim of the method for treating suspended wastewater from wet scrubbers, resulting from the wet separation of the solid phase from gas, is to achieve a closed scrubbing circuit. Insoluble particles are separated from the suspended wastewater stream from the scrubbing and the cleaned wastewater is returned to the scrubbing. The method is carried out on a device where a separator, for example a lamellar settler or a centrifuge, is included after the wet scrubber and the auxiliary tank, which is connected to a clear water tank and a recirculation pump. The use of both devices enables the production of a highly concentrated concentrated salt solution from wet scrubbers by better utilizing the low-potential waste heat of dusty exhalations without the risk of clogging or clogging of the supply lines, nozzles and scrubber stages, which, in addition to increasing operational reliability, also creates the prerequisite for the emergence of waste-free technology at technological nodes for the removal of dusty exhalations from wet scrubbers.
Description
CS 272 000 B1CS 272 000 B1
Vynález sa týká epósobu spracovania suspenzých odpadných vod z.mokrých pračiek azáriadenia k Jeho prevedeniu. V priemyselnej praxi sa často střetáváme so zachytáváním prašných exhalátov rozné-ho druhu. Prašné exhaláty sú vlastně zmesou Jemného prachu nejakej látky, alebo zmesilátok /solí/, so vzduchom, resp. s iným plynom /ddisik, argon, spaliny a pod./. Na hru-bé edlúčenie prachu od plynnej fázy sa používajú tzv. suché aeparátory, ako napr. cykló-ny, tkaniuové filtre, elektrofiltre a pod. Ak chceme zachytit všetok prach, musime po-užit tzv. mokré odlučovače, ako sú pračky venturiho typu, etážové a pod.BACKGROUND OF THE INVENTION The present invention relates to a process for treating slurry effluent from wet asparagus scrubbers. In industrial practice, we often encounter the capture of dusty exhales of various kinds. Dust exhales are actually a mixture of a fine dust of a substance, or a mixture of mixtures / salts /, with air, respectively. with other gas / ddisik, argon, flue gas and the like /. So-called dry aeparators such as cyclones, weave filters, electrofilters, and the like, are used to roughly separate dust from the gas phase. If we want to catch all the dust, we have to use so-called wet separators, such as venturi-type washing machines, trays and so on.
Mbkré pračky pracujú na principe priameho styku vypieracej vody a/alebo roztokus prašnými exhalátmi. Nevýhodou mokrých pračiek Je však, že produkujú relativné velkémnožstvo tzv, suepenzných odpadných vid, ako produkt vypierania. Aby sa minimalizovalomnožstvo týchto ýod, vačšina mokrých pračiek má tzv. vnútornú recirkuláciu, čoho podsta- * tou Je, že část suspenzných vod z vypierania sa vracia spát na skrápania a len.část saodvádza v podobě odpadných. suspenzných vod. Ak vypieraný prach obsahuje aj nerozpustnésoli popři rozpustných, alebo Je celkom nerozpustný /napr. sadze, popolčok/ vnútornúrecirkuláciu na pračke nie Je možné prevádzkovat, alebo len v malej miére z tohoto do-vodu, že v recirkulovanom roztoku obsiahnutá nerozpustná tuhá fáza zanáša privodné ha- > dice a trysky pračiek /u venturiho pračkách/, alebo etáže pračjlek etážových, čím vyřa-dí pračku z prevádzky, ktoráse potom naviac musí pracné čietit. Z uvedeného d&vodutakéto pračky vypierajúce nerozpustné, resp. čiastočne rozpustná prachy nemožno pre-vádzkovat s tzv. vnútornou recirkuláciou, čoho dosledkom Je, že vypiera^ suspenznýroztok ea len v malej miere zahusti /3 - 10 %/, čo znemožňuje vracanietýchto vod doprocesu, připadne iné využitie, právě prs vysoký obsah vody, resp. nizku koncentráciusoli. Tepelná spracovanie zahuštěném Je preto nerentabilné, Preto vo vačšine prlpadovtieto suspenzné vody sú vypúštané do kanálizacie. Ak vypieraný prach či soli sú zdra-viu škodlivými látkami, ale přitom sú cenné /ako napr. pri vypiarani prašných exhalá-tov pri výrobě hnojiv/ vzniká dvojnásobná škoda pri kanalizácii týchto vod tým, žeJednak znečistujú rieky a Jednak sa stráca inak cenný výrobok /napr. hnojivo/.Soft scrubbers work on the principle of direct contact of scrubbing water and / or solution with dusty exhalations. The disadvantage of wet scrubbers However, they produce a relatively large amount of so-called suepenzné waste, as a product of scrubbing. In order to minimize the amount of these scrubbers, most wet scrubbers have so-called internal recirculation, as a result of which part of the scrubbing water returning to sleep for scrubbing, and only part of it being discharged. suspension waters. If the scrubbed dust also contains insoluble salts or soluble, or is completely insoluble (e.g. the soot, ash / internal recirculation on the washing machine cannot be operated, or only to a small extent, that the insoluble solid phase contained in the recirculated solution entrains the feed hoses and the washing machine nozzles / in the venturi washers / or the storey racks thereby removing the washing machine from operation, which in addition must be laborious to read. From this d & partially soluble powders cannot be operated with so-called internal recirculation, as a result of which they wash the suspension solution and only to a small extent (3 - 10%), which makes it impossible to return to the process water, possibly to other uses, just the high water content, resp. low concentration. The thickened heat treatment is therefore unprofitable, therefore, in most of the slurry water, it is discharged into the channel. If the dust or salts washed out are harmful to health, but are valuable (such as in the case of dusty exhalations in the production of fertilizers), there is a double damage in the drainage of these waters by simply polluting the rivers and losing another valuable product. e.g. fertilizer /.
Vyššie uvedené nedostatky sú odstránená podlá vynálezu, podstatou ktoráho Je, žesuspenzné odpadnó vody z mokrých pračiek, v ktorých vypisrané prašné exhaláty sú skrá-pané čerstvou vodou, a/alebo roztokom čerstvej vody a suepenzných vod z prania, pri- ·'< Čom z prúdu suspenzných vod z prania sa oddslia nerozpustná částice, s výhodou odstře-děním alebo eedimentáciou, a vyčištěné vody sa vracajú spát na pranie. Zariadenia Á i k prevedeniu, pozostávajúce z mokrej pračky a pomocnej nádržky Je charakteristickétým, že za pomocnou nádržkou je zaradený kontinuálny separátor a zásobník čirých vod,ktorý Js spojený csz cirkulačnó čerpadlo a pomocnú nádržku s mokrou pračkou.The aforementioned drawbacks are eliminated according to the invention, the essence of which is the wastewater effluent from wet scrubbers, in which the printed dust extracts are scraped with fresh water and / or a solution of fresh water and wash water from washing. the flow of the slurry water from the washing is sifted off the insoluble particles, preferably by centrifugation or eedimentation, and the purified water is returned to the wash. A device for design, consisting of a wet scrubber and an auxiliary reservoir is characterized by a continuous separator and a clear water reservoir being connected downstream of the auxiliary reservoir, which is connected to a circulation pump and an auxiliary reservoir with a wet scrubber.
Ako kontinuálny separátor sa s výhodou použije lamelový usadzovák a/alebo odstředivka. Výsledkom uplatnenia tohoto sposobu a zariadenia je ziskanis vysoko zahuštěnéhosuspenzného roztoku, ktorý sa získá priamym zahuštěním na pračke, na úkor lepšiehovyužitia nízkopotencionálneho odpadného tepla prašných exhalátov a následnou separá- ’ ciou na kontinuálnom usadzováku a/alebo odstředivka. Takto získaný vysoko zahuštěnýsuspenzný roztok sa už dá energeticky výhodné zahustit /prs nizky obsah vody/ a/alebovrátit do výrobnóho procesu.Preferably, a continuous lamella settler and / or centrifuge is used as a continuous separator. As a result of the application of this method and apparatus, a highly thickened suspension solution is obtained, which is obtained by direct thickening on a washing machine, at the expense of a better utilization of low-potential waste heat of dust particles and subsequent separation on a continuous settler and / or centrifuge. The highly thickened suspension solution thus obtained can already be energetically thickened (low water content) and / or returned to the manufacturing process.
Nový.a vyšší účinok sposobu spracovania suspenzných odpadných v3d z mokrých pra-čiek a zariadenia k Jeho prevedenija podlá vynálezu spočívá v možnosti ziskania vysokozahuštěného suspenzného roztoku soli z mokrých pračiek, lepším využitím vlastníhonízkopotencionálneho odpadného tepla prašných exhalátov bez nebezpečia zanášania,resp. upchatia prívodných trás, trysiek a etá.žl pračiek, čím okrem zvýŠenia prevádzko- " ? ' - ;'ΐ /ΐϊίίί í :í s íThe new and higher effect of the process of treating slurry wastewater from wet scrubbers and apparatuses according to the invention consists in the possibility of obtaining a high-density suspension solution of salt from wet scrubbers, by better utilization of the self-propelled waste heat of dusty exhalations without the risk of clogging, respectively. clogging of supply lines, nozzles, and washing machine racks, in addition to increasing traffic - "-"
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Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS873315A CS272000B1 (en) | 1987-05-08 | 1987-05-08 | A method of treating sludge wastewater from wet scrubbers and apparatus for its operation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS873315A CS272000B1 (en) | 1987-05-08 | 1987-05-08 | A method of treating sludge wastewater from wet scrubbers and apparatus for its operation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CS331587A1 CS331587A1 (en) | 1988-06-15 |
| CS272000B1 true CS272000B1 (en) | 1990-12-13 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS873315A CS272000B1 (en) | 1987-05-08 | 1987-05-08 | A method of treating sludge wastewater from wet scrubbers and apparatus for its operation |
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| Country | Link |
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| CS (1) | CS272000B1 (en) |
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1987
- 1987-05-08 CS CS873315A patent/CS272000B1/en unknown
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| Publication number | Publication date |
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| CS331587A1 (en) | 1988-06-15 |
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