Thursday, March 11, 2010

Stainless Steel Condensate Polisher with Bray Valves

Res-Kem just completed another condensate polisher manufactured in stainless steel. This system uses our standard design with optional butterfly valves.


The vessel is manufactured from 304L stainless steel with 100 psi ASME code construction. Pipe assemblies are welded Schedule 10 304L stainless steel piping. This single unit condensate polisher has an added feature of automatic bypass. The customer required our optional Bray butterfly valve design.

The actuators are air open/spring return so the valves can work with the GE Aquamatic 962 series stager controller.

Regeneration is initiated by either:
  • Gallon throughput

  • High differential pressure

  • Timeclock

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Wednesday, March 03, 2010

Blogger Transition from FTP-Step #7

While everything looked fine at first, it turns out there was one more big problem we had in our transition from our own hosted blog using FTP with Blogger to a Blogger hosted blog. The numerous pictures we had in our old posts were not showing up in our Blogger hosted version. It turned out a step 7 required to make the final transition.

After searching Blogger Help and hunting around we found this paragraph at the bottom of the page:

"This situation may arise if you originally published your blog via FTP and then switched to using custom domain publishing. Images originally posted to your server do not get transferred over to Blogger when you do this, so you may want to move them all to a server such as images.yourdomain.com and use that as your missing files host."

Blogger did not make this easy because I needed to make a new server, so I had to contact LinuxForce to help us one more time.

I think finally I am out of the woods on this transition! Now I can get back to my routine blogs on water treatment systems, news, innovation and technology.

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Thursday, February 25, 2010

Shut-Down of FTP Support on Blogger - Step 6

Well, I had to invoke step #6 "Have a good resource to call if this does not work!!". While the transition was smoother than I anticipated, I still needed a couple of redirect statements to solve some broken links and "Page Not Found" errors. The group helping me to get my Blogger account transitioned is LinuxForce. They verified what to do, gave me the simple steps required and made server and minor site adjustments. I am very satisfied!

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Shut-Down of FTP Support on Blogger-Steps 3-5

Well, I think we might be okay. We need to do Step #5 with our web hosting support person later today. I could do it, but I'll let them. The next step will be to check links and history. Hopefully I will not need to employ Step #6 "Have a good resource to call if this does not work!!"

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Shut-Down of FTP Support on Blogger

You may have seen a hiatus with my normally routine blog posts. I was a little preoccupied this past month. I was in a crisis about a imminent shutdown of FTP support on Blogger, the application we have been using to post our blogs.


Situation:

We recently announced that our blog on water treatment is approaching its 4th year. Almost simultaneously, we were sent an email from the Blogger Product Manager announcing "a planned shut-down of FTP support on Blogger Buzz (the official Blogger blog), and wanted to make sure you saw the announcement". Not having the time, nor frankly the interest in following a Blogger blog on blogging support, we did not see it until the email on February 2, 2010. The clock was ticking so I needed to find out what to do and how implement a solution by March 26, 2010.


Main Challenges:

I am pretty savvy technically, but this one required some research. The main challenges were:

  • Using FTP to post our blog has been relatively painless.

  • Retaining the numerous links to and from Blogger to www.reskem.com and other sites.

  • Losing our over 100 posts on our blog and/or having two locations were the blog resides

  • Losing our daily automatic backup of our blog during our normal, automatic website backup

  • Having to structurally change our website, http://www.reskem.com/

  • Needing to change settings at our web hosting company that they may or may not be able/willing to do

  • Losing our search rankings because of this substantive change in hosting from our server to a Blogger (Google) server

Some of the Research:

I read many articles on the web and in several recent books on possible blog posting software applications and strongly considered changing. A posting on Blogger Buzz seemed to indicate a smooth transition, but there were some server settings, redirects, and files required that I was unwilling/unable/scared to undertake on my own. Luckily my web hosting company has an excellent resource to walk me through the process.


Process:

Here was the process to make the transition:

  1. Set up http://blog.reskem.com/ in DNS

  2. Wait a day (This is the set I am at now)

  3. Follow instructions to "Update Your Blogger Settings" using blog.reskem.com as the "Custom Domain"

  4. Check to see if it works by navigating to http://blog.reskem.com/

  5. Set up an .htaccess file to redirect traffic from http://www.reskem.com/blog/ to http://blog.reskem.com/

  6. Have a good resource to call if this does not work!!

Since I am at step #2 going to start step #3, we'll see if this blows up and I lose 4 years of work!


Why did Blogger decide to do this?

Here is some additonal text from the announcment email. It sounds valid, but still a pain for us at Res-Kem:

"Last May, we discussed a number of challenges facing[1] Blogger users who relied on FTP to publish their blogs. FTP remains a significant drain on our ability to improve Blogger: only .5% of active blogs are published via FTP — yet the percentage of our engineering resources devoted to supporting FTP vastly exceeds that. On top of this, critical infrastructure that our FTP support relies on at Google will soon become unavailable, which would require that we completely rewrite the code that handles our FTP processing.

Three years ago we launched Custom Domains[2] to give users the simplicity of Blogger, the scalability of Google hosting, and the flexibility of hosting your blog at your own URL. Last year's post discussed the advantages of custom domains over FTP[3] and addressed a number of reasons users have continued to use FTP publishing. (If you're interested in reading more about Custom Domains, our Help Center has a good overview[4] of how to use them on your blog.) In evaluating the investment needed to continue supporting FTP, we have decided that we could not justify diverting further engineering resources away from building new features for all users."

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Tuesday, January 26, 2010

Automatic DI Bank Switching and Data Acquisition Controller


Res-Kem has developed an integrated DI Bank Switching and Data Acquisition Automation Controller. The system monitors the inlet and outlet resistivity and the flow rate. At one of several alarm points, the system will send a text message to any number of email addresses and mobile devices. As part of a service agreement with Res-Kem/General Water, the system will warn Res-Kem/General Water personnel to prepare for a replacement of the soon to be exhausted bank of DI bottles.

Depending upon the system programming the bank will attempt to rinse to quality in several stages. If it does not succeed, the bank will switch to a standby bank and notify Res-Kem that the bank is exhausted fully and needs to be changed out.

The reason why Res-Kem developed this product is many people were having problems getting replacement parts and proprietary circuit boards for the excellent product called the Aquaswitch II a registered trademark of Myron L. Also, with reduced staffing at most of our customers, people do not have the time to monitor a stack light or resistivity monitor. As a result, the quality can be poorer than required potentially damaging down stream processes and products.

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Friday, January 15, 2010

Tiny Particles Fight Giant Water Problem

Many of you may have heard of the chemicals that are in our drinking water including drugs, antibiotics, and other very small and difficult to remove chemicals. These can cause health effects at very low levels. Some disrupt the hormone systems of humans and wildlife, posing threats to fetal development and young children. Sources include birth control pills, prescription drugs, antibiotics, cosmetics and fragrances. People take the drugs and excrete them in urine.

In the online article "Pollutant-Fighting Particles Purify Water" in Lab News Daily by Laboratory Equipment, it briefly describes the continuing R&D project by two Charlton University professors to bring this technology to municipal and industrial waste water treatment plants. It will be interesting to see how they plan on removing the particles from the treated waste water in a cost-effective manner.

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Tuesday, January 12, 2010

Deionizer/Demineralizer System with Packaged Design Introduced


Res-Kem recently introduced packaged DI Water Systems for Commercial and Light Industrial applications. The OHM-TECH Series two-bed deionizers for commercial and light industrial applications are designed for semi-automatic production of water with a conductivity of less than 10 micro-ohms and feature:

  • Flow rates from 1 - 40 gpm
  • Ion exchange Capacities from 9,000 - 90,000 grains.
  • Strong acid cation and type 1 strong base anion resins.
  • Microprocessor based control system with conductivity monitor and flow sensor for regeneration initiation.
  • Corrosion resistant fiberglass electrical enclosures which reduces maintenance costs.
  • Resin vessels are polyethylene-lined fiberglass.
  • ASME code vessels.
  • Factory assembly and skid mounting for quick installation and minimum startup cost.
  • Schedule 80 PVC piping package using a multi-function hydraulically operated composite valve.
  • Metering valves for accurate and safe control of regeneration water and chemical introduction.
  • Internal distributors are corrosion resistant, designed for optimum efficiency.

These following facilities are examples of ideal applications for Res-Kem's demineralizer and deionizer (DI) equipment:

  • Food and Beverage Processing Plants
  • Power plants
  • Chemical plants
  • Pharmaceutical Plants
  • High pressure boiler feedwater
  • Manufacturing Plants
  • Laboratories
  • Autoclaves
  • Steam Generators
  • Electronic Products
  • Medical Device Production
  • Alloy Metal Fabrication
  • Aerospace
  • Humidification Systems
  • Metal Treating
  • Plating
  • Printed Circuit Boards

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Tuesday, December 22, 2009

"Toxic Waters" Article From The New York Times

An excellent article on water quality in the United States entitled "Toxic Waters" , was published by the NY Times on December 16, 2009. The premise of the article is that just because a water is "legal" it may not be "healthy". Our policy is not to be a fear monger, but the article was very concerning.

A very interesting part of this article was the water quality data for each State. The amount of data is mind boggling! The data was collected and analysed by the Environmental Working Group who shared it with The New York Times.

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Wednesday, December 02, 2009

Dealkalizer Performance Calculations

We recently had questions about a perceived problem with a dealkalizer. This customer believed the capacity of the dealkalizer was lower than originally specified and was unhappy with its performance. The customer was regenerating this new system more often than they regenerated the older system. We reviewed the system design and operation and found the problems.

Determining the Dealkalizer Capacity:
In order for us to know how long a dealkalizer system will produce dealkalized water between regenerations, we need a complete water analysis. There are a number of factors in determining the capacity of Dealkalizer Systems. The two most important things used to determine resin capacity are: Influent TDS and Alkalinity (as a percentage of the TDS). Once these are known, the resin capacity can be determined by using established resin manufacturers' charts, or by doing calculations based on total exchangeable anions and percentages of alkalinity and chlorides.

Based on using the charts and info from Purolite and Rohm & Haas

Purolite A-300 Strong Base Anion Resin Dealkalizer Capacity Curves the capacity they should be getting is approximately 2,900 grains/cu ft x 15 cu ft = 43,500 grains removal. With 50 ppm (2.93 grains/gallon) alkalinity, this equates to 14,846 gallons between regenerations.

Minimum Flow Rate:
This capacity is further based on the flow rate of the system. Ideally, the unit should run @ 2 gpm/cu ft of resin or 30 gpm. Further, the minimum flow rate to insure proper kinetics and to prevent channeling is 2 gpm/sq ft of tank surface area. In their case, with a 30" diameter fiberglass tank, which has a surface area of 4.6 sq ft, the minimum flow rate should be 9.2 gpm.

We advised the customer that their average real time flow rate is 271 gph, which is 4.5 gpm. This is well below the recommended flow rate of 9.2 gpm. At this rate, the water is definitely channeling resulting in premature alkalinity breakthrough.

Premature alkalinity breakthrough would necessitate regenerating the system more often. If the dealkalizer was being run at the design rate of 9.2 gpm it would regenerate less often.

Resin Regeneration Frequency and Resin Life:
Before this customer understood the cause of the dealkalizer problem he was concerned the dealkalizer resin had lost its original capacity. Furthermore he was concerned that regenerating the dealkalizer more often would affect the life of the resin. The answer in both cases was no. The resin was in good shape and regenerating the system more often would not be detrimental to it.

Their very old dealkalizer did not appear to regenerate as often as the new system. There could have been any number of reasons it didn't.

  • Was it actually producing dealkalized water in the 5 ppm range?
  • Was the resin broken down to the point where it could operate at low flows and still work?
  • Is the water analysis from 2008 the same as now?

We don't know the answers to the first two questions but it's very doubtful that the analysis is the same, as water in most areas can change dramatically from summer to winter and from drought to rainy times. We asked them to check the water in the winter when there is a lot of snow and/or ice. The salt on the roads increases the TDS of the water, not to mention the alkalinity and chlorides; all of which will have a significant affect on the performance of a dealkalizer.

Solutions and Recomendations:

Adding Caustic to Salt During Regeneration Increases Resin Capacity
They may be able to increase the capacity of the dealkalizer somewhat by increasing the amount of the salt and caustic. However, it may not be worth it given the low flow rate of operation.

We don't feel making changes to the dealkalizer will enable it to produce more treated water between regenerations. If the real time flow will continue at 4.5 gpm (or less), we suggested they installation of a recirculation pump on the softener/dealkalizer system. This will insure there is enough water going through the units and prevent channeling.

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