Philip Morris
Summary of Wel-2 Clean-Up Meeting - 920611
Fields
- Author
- Donaher, D.R.
- Shakeri, S.Z.
- Area
- JENKINS,DEBBIE/OFFICE
- Type
- MEMO, MEMORANDUM
- MINU, MINUTES
- Recipient (Organization)
- Park 500
- Named Person
- Sharkey, J.J.
- Barfield, D.L.
- Clark, D.A.
- Bailey, W.H.
- Braun, K.G.
- Brown, J.S.
- Bullock, T.J.
- Donaher, D.R.
- Fox, L.J.
- Saunders, D.
- Shakeri, S.Z.
- Recipient
- Saunders, D.
- Document File
- 2024794524/2024794872/Sp Operating Problems Worklife
- Issues Principles Nonconformances
- 2024794525/2024794605/Cp Operating Problems
- Author (Organization)
- Park 500
- Named Organization
- Eng Eq
- Hycor
- Litigation
- Stmn/Produced
- Characteristic
- MARG, MARGINALIA
- Site
- M45
- Master ID
- 2024794531/4536
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P A R R 5 0 0'
I N T E R - O F F I C E C O R R E S P O N D E N C E
Chester, Virginia
phil a/
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To: Dawn Saunders Date: June 1~5, 'l~SW,qeC
From: ~ Sheida Shakeri/Denise Donaheri)vb
Subject: Summary of WEL-2 Clean-up Meeting - June 11, 1992
Meeting Objectives
1) To review background and status of WEL-2 clean-up project
2) To discuss issues to be resolved and action plan for
completion~ of the project
Attendance
W. H. Bailey D. R. Donaher
O:UL~'~~`arfleld~( absent)- L. J. Fox
K. G. Braun D. C. Saunders
J. S. Brown S. Z. Shakeri
T. J. Bullock J. J. Sharkey
D. A. Clark (absent)
Background
*
Original project justification was to reduce RBW overflow by
replacing 12 gpm of fresh water (TME shower & HDC elutriation)
with filtered WEL-2 for yield improvement.
X Initial testing of Rotoshear on a HRS-2448 (small experimental
unit) with a 0.005"1 screen in: 1986, was aimed~ at evaluation of
fiber removal on various liquor streams throughout the process
(WEL-2 was not tested).
* Successful test results led to the installationi of another
HRS-2448 unit with a 0.005" screen in 1989 over the #1 blend
pulper in Line 3 Blending, for evaluation of fiber removal for
WEL-2 clean-up to replace fresh water. (The WEL-2 maximum
throughput flows were not tested during experimental unit
evaluation in 1989.)
* The unit performed satisfactorily in fiber removal and
therefore the recommendation was made to install a permanent
WEL-2 clean-up system for filtering all the WEL-2. flow (90-12&
gpm).

(continued)
----
* Co Design criteria communicated from Park 500 to Phj~~p fident;al
Eng. Eq. Co./Hycor in January 1990 included WEL-2 f1Tdi~
requirements of 90-120 gpm and 0.005" screen, which were '6eC
written memos. Additional design criteria such as liquor
consistency, temperature and flowrate were communicated
orally.
* Hycor made the proposal and recommend'ation for installation of
a HRS-3672 (large scale unit) to meet given design criteria.
(No specific performance guarantee was included.)
Status
* System start-up indicated insufficient WEL-2 flow through~the
HRS-3672 unit in Line 3 Stock Prepy resulting in! the inability
to maintain level in the HWEL tank.
* Repeated testing of the HRS-3672 unit has revealed that the
maximumthroughput is about 50 gpm, for WEL-2 (vs. design
requirement of 90-120 gpm) with unacceptable frequency of
shower usage to keep the screen clean.
* Investig,ation into the causes for performance failure of the
HRS-3672 unit, has determined usage of incorrect design
criteria. The primary design criteria used by Hycor for
sizing the unit was a maximum flowrate of 50 gpm for SEL on
the HRS-2448 unit, based on 1986 SEL testing. May 1991
testing on WEL-2 showed that the actual maximum throughput for
WEL-2 is 15 gpm on the HRS-244'8 unit.
Hydraulic testing of our HRS-3672 unit, performed by Hycor,
has verified'the accuracy of their hydraulic design. The
design problem lies with usage of inappropriate process stream~
throughput data for designing the unit.
* Original 650 committed $175,000 for the project with
approximately $200,000 spent.
Issues
* Unacceptable frequency of shower usage to prevent Hycor screen
from blinding
* Frequency determination of pluggage for the TME shower and the
TME/HDC rotameter
* Rotoshear Headbox design
* Justification for cleaning all the WEL-2 (vs. 12 gpm required
for TME shower & HDC elutriation)i

r
('continued)i Cohrii ~e
philRtiat
Can, the expected yield'~ improvement be substan ~~egS KABC
this time,i.e.,does the project as scoped in Jan,1991
have justification currently?
Action Plan
* Schedule a fact finding meeting with Eng. Eq,. Co/Hycor
representatives to assess liability for the design criteria
and the resulting failure of the HRS-3672 unit to perform as
required. Specific questilons for the meeting will be prepared
by 6/18/92 for review.
* If a different unit is required or modifications are needed~
for our existing, unit to complete the WEL-2 project, a
performance guarantee will be pursued.
* Additional inputs oni the past performance of HRS-2448 unit ini
Blending will be solicited to, determine frequency of pluggage
for the TME shower, TME & HDC rotometers, and the Hycor
screen.
* Relocate HRS-2448'unit back to Line 3 Blending to repeat 1990
testing in a structured plan. A detailedevaluation plan will
be prepared.
